EP1736490A2 - Polymer blend based on polycarbonate polyols - Google Patents
Polymer blend based on polycarbonate polyols Download PDFInfo
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- EP1736490A2 EP1736490A2 EP06012152A EP06012152A EP1736490A2 EP 1736490 A2 EP1736490 A2 EP 1736490A2 EP 06012152 A EP06012152 A EP 06012152A EP 06012152 A EP06012152 A EP 06012152A EP 1736490 A2 EP1736490 A2 EP 1736490A2
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- polyurethane
- coating compositions
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/2805—Compounds having only one group containing active hydrogen
- C08G18/2815—Monohydroxy compounds
- C08G18/283—Compounds containing ether groups, e.g. oxyalkylated monohydroxy compounds
- C08G18/2835—Compounds containing ether groups, e.g. oxyalkylated monohydroxy compounds having less than 5 ether groups
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/0804—Manufacture of polymers containing ionic or ionogenic groups
- C08G18/0819—Manufacture of polymers containing ionic or ionogenic groups containing anionic or anionogenic groups
- C08G18/0823—Manufacture of polymers containing ionic or ionogenic groups containing anionic or anionogenic groups containing carboxylate salt groups or groups forming them
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/0804—Manufacture of polymers containing ionic or ionogenic groups
- C08G18/0819—Manufacture of polymers containing ionic or ionogenic groups containing anionic or anionogenic groups
- C08G18/0828—Manufacture of polymers containing ionic or ionogenic groups containing anionic or anionogenic groups containing sulfonate groups or groups forming them
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/0838—Manufacture of polymers in the presence of non-reactive compounds
- C08G18/0842—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents
- C08G18/0861—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers
- C08G18/0866—Manufacture of polymers in the presence of non-reactive compounds in the presence of liquid diluents in the presence of a dispersing phase for the polymers or a phase dispersed in the polymers the dispersing or dispersed phase being an aqueous medium
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
- C08G18/12—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step using two or more compounds having active hydrogen in the first polymerisation step
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
- C08G18/4018—Mixtures of compounds of group C08G18/42 with compounds of group C08G18/48
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
- C08G18/4205—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups
- C08G18/4208—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups
- C08G18/4211—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols
- C08G18/4216—Polycondensates having carboxylic or carbonic ester groups in the main chain containing cyclic groups containing aromatic groups derived from aromatic dicarboxylic acids and dialcohols from mixtures or combinations of aromatic dicarboxylic acids and aliphatic dicarboxylic acids and dialcohols
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/40—High-molecular-weight compounds
- C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
- C08G18/44—Polycarbonates
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
- C08G18/66—Compounds of groups C08G18/42, C08G18/48, or C08G18/52
- C08G18/6633—Compounds of group C08G18/42
- C08G18/6637—Compounds of group C08G18/42 with compounds of group C08G18/32 or polyamines of C08G18/38
- C08G18/664—Compounds of group C08G18/42 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203
- C08G18/6644—Compounds of group C08G18/42 with compounds of group C08G18/32 or polyamines of C08G18/38 with compounds of group C08G18/3203 having at least three hydroxy groups
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
- C08G18/65—Low-molecular-weight compounds having active hydrogen with high-molecular-weight compounds having active hydrogen
- C08G18/66—Compounds of groups C08G18/42, C08G18/48, or C08G18/52
- C08G18/6633—Compounds of group C08G18/42
- C08G18/6659—Compounds of group C08G18/42 with compounds of group C08G18/34
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
- C08G18/703—Isocyanates or isothiocyanates transformed in a latent form by physical means
- C08G18/705—Dispersions of isocyanates or isothiocyanates in a liquid medium
- C08G18/706—Dispersions of isocyanates or isothiocyanates in a liquid medium the liquid medium being water
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
- C08L75/02—Polyureas
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L75/00—Compositions of polyureas or polyurethanes; Compositions of derivatives of such polymers
- C08L75/04—Polyurethanes
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D175/00—Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
- C09D175/04—Polyurethanes
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
- C09D175/00—Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
- C09D175/04—Polyurethanes
- C09D175/06—Polyurethanes from polyesters
Definitions
- the invention relates to aqueous coating compositions based on polycarbonate polyols, a process for their preparation and use as a soft-feel coating.
- PU dispersions Polyurethane-polyurea dispersions
- aqueous formulations of PU dispersions are known in the art.
- An important field of application of aqueous preparations of ionically modified PU dispersions lies in the area of the coating of plastic parts.
- plastic parts are usually painted to protect the plastic from external influences, such as sunlight, chemical, thermal and mechanical stress, to achieve certain hues and color effects, to cover defects of the plastic surface or to the plastic surface a pleasant grip To give (haptic).
- softfeel paints are increasingly used in recent years.
- "Softfeel effect" in the sense of the present invention denotes a special feel (feel) of the painted surface; This feel can be described in terms of velvety, soft, rubbery, warm.
- aqueous softfeel lacquers based on polyurethane chemistry have become established in recent years, as exemplified in US Pat DE-A 44 06 159 be revealed.
- these coatings also give coatings with good resistance and protective effect for the plastic substrate. In the meantime, however, it has been shown that these lacquers and coatings often have inadequate resistance to hydrolysis.
- the object of the present invention was therefore to provide coating compositions which, in addition to the o.g. mechanical and haptic properties, compared to prior art coating compositions, lead to significantly more hydrolysis-stable coatings.
- plastic coating compositions with the desired haptic Softfeel properties consist of a part of polyurethane dispersions that have no appreciable amounts of hydroxy-functional groups.
- DE-A 101 22 444 describes hydrolystable, ionically and / or nonionically hydrophilicized polyurethane-polyurea- (PUR) -dispersions based on polycarbonate polyols and polytetramethylene glycol polyols.
- PUR polyurethane-polyurea-
- the dispersions lead to a variety of substrates in one-component Coating agents for hydrolysis-stable, kink- and scratch-resistant coatings. However, an application of these dispersions as softfeel paints is not described.
- aqueous two-component (2K) coating compositions containing both non-functional PUR polymers based on specific polycarbonate polyols and hydrophilic, hydroxyl-containing PUR polymers based on specific polycarbonate polyols exhibit excellent hydrolytic stability and at the same time the desired haptic properties.
- Suitable polyisocyanates of component A.1) are the aromatic, araliphatic, aliphatic or cycloaliphatic polyisocyanates of an NCO functionality known per se to the person skilled in the art of preferably ⁇ 2, which may also have iminooxadiazinedione, isocyanurate, uretdione, urethane, allophanate, biuret, urea, oxadiazinetrione, oxazolidinone, acylurea and / or carbodiimide structures. These can be used individually or in any mixtures with each other.
- polyisocyanates examples include hexamethylene diisocyanate (HDI), isophorone diisocyanate (IPDI), the isomeric dicyclohexylmethane-4,4'-diisocyanate or mixtures thereof of any isomer content and 1,4-cyclohexyl diisocyanate.
- HDI hexamethylene diisocyanate
- IPDI isophorone diisocyanate
- IPDI isophorone diisocyanate
- the isomeric dicyclohexylmethane-4,4'-diisocyanate or mixtures thereof of any isomer content and 1,4-cyclohexyl diisocyanate examples include hexamethylene diisocyanate (HDI), isophorone diisocyanate (IPDI), the isomeric dicyclohexylmethane-4,4'-diisocyanate or mixtures thereof of any isomer content and 1,4-cyclohexy
- non-modified polyisocyanate having more than 2 NCO groups per molecule see e.g. 4-Isocyanatomethyl-1,8-octane diisocyanate (nonane triisocyanate) called.
- hexamethylene diisocyanate isophorone diisocyanate, the isomeric dicyclohexylmethane-4,4'-diisocyanate and mixtures thereof.
- Hydroxyl-containing polycarbonate polyols are obtainable by reaction of carbonic acid derivatives, for example diphenyl carbonate, dimethyl carbonate or phosgene with diols.
- the hydroxy-functional polycarbonate polyols A.2) to be used according to the invention have an average hydroxyl functionality of 1.6 to 4, preferably 1.8 to 3 and particularly preferably 1.9 to 2.3 and a number-average molecular weight of 240 to 8000 g / mol from 500 to 3000 g / mol, more preferably from 750 to 2500 g / mol.
- the preparation of the polycarbonate polyols is preferably carried out according to the in the EP-A 1 404 740 (Pp. 6-8, examples 1-6) and EP-A 1 477 508 (Page 5, Example 3) described manufacturing method.
- diols come e.g. 1,3- and 1,4-butanediol, 1,6-hexanediol, 1,8-octanediol, 1,12-dodecanediol, neopentyl glycol, 1,4-bis-hydroxymethylcyclohexane, 2-methyl-1,3-propanediol and trimethylpentanediol-1 , 3 in question, wherein the proportion of 1,4-butanediol is at least 25 wt .-% of the diol components used.
- the diol component preferably contains 45 to 100% by weight 1,4-butanediol, and 0 to 55% by weight 1,6-hexanediol, particularly preferably 60 to 100% by weight 1,4-butanediol and 0 to 40% by weight .-% 1,6-hexanediol.
- the hydroxylpolycarbonates are preferably linear, but may optionally be branched by the incorporation of polyfunctional components, in particular low molecular weight polyols.
- Particularly preferred components A.2) are based on mixtures of 1,4-butanediol and 1,6-hexanediol and have an average hydroxyl functionality of 1.9 to 2.05.
- Polyester polyols which have a molecular weight Mn of from 400 to 6000 Da, more preferably from 600 to 3000 Da, can likewise be used as polymeric polyols A.2).
- Their hydroxyl number is generally 22 to 400 mg KOH / g, preferably 50 to 200 mg KOH / g and more preferably 80 to 160 mg KOH / g, and have an OH functionality of 1.5 to 6, preferably 1.8 to 4, and more preferably from 1.9 to 3.3.
- Suitable dicarboxylic acids are preferably phthalic acid, isophthalic acid, terephthalic acid, tetrahydrophthalic acid, hexahydrophthalic acid, or adipic acid.
- Anhydrides of these acids are also suitable, as far as they exist. As a result, for the purposes of the present invention, the anhydrides are encompassed by the term "acid”.
- Monocarboxylic acids such as benzoic acid and hexanecarboxylic acid can also be used, provided that the average functionality of the polyol is higher than 2.
- trimellitic acid may be mentioned here.
- suitable components A.2) are the polylactone and polyether polyols known from polyurethane chemistry, insofar as they correspond to the abovementioned criteria in terms of functionality and molecular weight.
- the proportion of the hydroxyl polycarbonates in the sum of the polyols used from A.2) for the preparation of the polymers (I) or (II) is 35 to 100 wt .-%, preferably 45 to 100 wt .-% and particularly preferably 65 to 100 wt .-%.
- the low molecular weight polyols A.3) used to build up the polyurethane resins generally cause stiffening and / or branching of the polymer chain.
- the molecular weight is preferably between 62 and 200 Da.
- Suitable polyols may contain aliphatic, alicyclic or aromatic groups. Mentioned here are, for example, the low molecular weight polyols having up to about 20 carbon atoms per molecule, such as.
- ethylene glycol diethylene glycol, 1,4-butanediol, 1,3-butylene glycol, cyclohexanediol, 1,4-cyclohexanedimethanol, 1,6-hexanediol and trimethylolpropane, glycerol or pentaerythritol.
- Di- or polyamines as well as hydrazides can also be used as A.3), e.g. Ethylenediamine, 1,2- and 1,3-diaminopropane, 1,4-diaminobutane, 1,6-diaminohexane, isophoronediamine, isomer mixture of 2,2,4- and 2,4,4-trimethylhexamethylenediamine, 2-methylpentamethylenediamine, diethylenetriamine, 1,3- and 1,4-xylylenediamine, ⁇ , ⁇ , ⁇ ', ⁇ '-tetramethyl-1,3- and 1,4-diaminodicyclohexylmethane, dimethylethylenediamine, hydrazine or adipic dihydrazide.
- compounds which contain active hydrogen with respect to NCO groups of different reactivity such as compounds which, in addition to a primary amino group, also have secondary amino groups or OH groups in addition to an amino group (primary
- the polyurethane resins I) and II) may also contain, if appropriate, building blocks A.4), which are located in each case at the chain ends and terminate them.
- building blocks are derived, on the one hand, from monofunctional compounds reactive with NCO groups, such as monoamines, in particular mono-secondary amines or monoalcohols.
- Preferred isocyanate-reactive groups are hydroxyl or amino groups.
- Suitable ionically or potentially ionically hydrophilizing compounds are, for example, mono- and dihydroxycarboxylic acids, mono- and diaminocarboxylic acids, mono- and dihydroxysulfonic acids, mono- and diaminosulfonic acids and also mono- and dihydroxyphosphonic acids or mono- and diaminophosphonic acids and their salts such as dimethylolpropionic acid, dimethylolbutyric acid, hydroxypivalic acid, N- (2-aminoethyl) - ⁇ -alanine, 2- (2-aminoethylamino) -ethanesulfonic acid, ethylenediamine-propyl- or -butylsulfonic acid, 1,2- or 1,3-propylenediamine ⁇ -ethylsulfonic acid, malic acid, citric acid, glycolic acid, lactic acid, glycine, alanine, taurine, lysine, 3,5-d
- ionic compounds A.5) which have carboxy or carboxylate and / or sulfonate groups and / or ammonium groups.
- Particularly preferred ionic compounds A.5) are those which contain carboxyl and / or sulfonate groups as ionic or potentially ionic groups, such as the salts of N- (2-aminoethyl) - ⁇ -alanine, the 2- (2-amino) ethylamino) ethanesulfonic acid or the addition product of IPDI and acrylic acid ( EP-A 0 916 647 Example 1) and the dimethylolpropionic acid.
- Suitable nonionic hydrophilic compounds according to the definition of component A.6) are e.g. Polyoxyalkylene ethers containing at least one hydroxy or amino group. These polyethers contain from 30% to 100% by weight of building blocks derived from ethylene oxide.
- the polyalkylene oxide polyether alcohols are either pure polyethylene oxide polyethers or mixed polyalkylene oxide polyethers whose alkylene oxide units consist of at least 30 mol%, preferably at least 40 mol%, of ethylene oxide units.
- Preferred nonionic compounds are monofunctional mixed polyalkylene oxide polyethers which have at least 40 mol% of ethylene oxide and not more than 60 mol% of propylene oxide units.
- PUR polymers (I) it is preferred to use a combination of ionic and nonionic hydrophilicizing agents according to the definitions of components A.5) and A.6). Particularly preferred are combinations of nonionic and anionic hydrophilicizing agents.
- component A.1 10 to 40% by weight of component A.1), 55 to 85% by weight of component A.2), 1 to 25% by weight of the sum of compounds A.3) and A.4) are particularly preferred, 0 to 10% by weight of component A.5), 0 to 10% by weight of component A.6), the sum of A.5) and A.6) being 0.1 to 20% by weight and the sum of all components added to 100 wt .-%.
- component A.1 Very particular preference is given to 15 to 40% by weight of component A.1), 60 to 85% by weight of component A.2), 1 to 20% by weight of the sum of compounds A.3), 0 to 8% by weight .-% Component A.5), 0 to 10 wt .-% component A.6) used, wherein the sum of A.5) and A.6) is 0.1 to 18 wt .-% and the sum of all components to 100 wt .-% added.
- the coating compositions according to the invention comprise PU polymers (I) which are used in the form of their aqueous PU dispersion (I).
- the process for the preparation of the aqueous PU dispersion (I) can be carried out in one or more stages in homogeneous or in multistage reaction, partly in disperse phase. After completely or partially carried out polyaddition from A.1) - A.6) takes place a dispersing, emulsifying or dissolving step. This is followed, if appropriate, by a further polyaddition or modification in disperse phase.
- aqueous polyurethane dispersions (I) all known from the prior art methods such as.
- Example, prepolymer mixing method, acetone method or Schmelzdipergiervon can be used.
- the PU dispersion (I) is preferably prepared by the acetone process.
- the components A.2) to A.6) which may have no primary or secondary amino groups and the polyisocyanate component A.1) for the preparation of an isocyanate-functional polyurethane Prepolymer presented in whole or in part and optionally diluted with a water-miscible but isocyanate-inert solvent and heated to temperatures ranging from 50 to 120 ° C.
- the catalysts known in polyurethane chemistry can be used. Preference is given to dibutyltin dilaurate.
- Suitable solvents are the usual aliphatic, ketofunctional solvents, e.g. Acetone, butanone, which can be added not only at the beginning of the preparation, but possibly also in parts later. Preferred are acetone and butanone.
- the molar ratio of isocyanate groups to isocyanate-reactive groups is 1.0 to 3.5, preferably 1.1 to 3.0, particularly preferably 1.1 to 2.5.
- reaction of the components A.1) - A.6) to the prepolymer takes place partially or completely, but preferably completely.
- polyurethane prepolymers containing free isocyanate groups are obtained in bulk or in solution.
- the partial or complete salt formation of the anionically and / or cationically dispersing groups takes place.
- bases such as tertiary amines, e.g. Trialkylamines having 1 to 12, preferably 1 to 6 carbon atoms used in each alkyl radical. Examples of these are trimethylamine, triethylamine, methyldiethylamine, tripropylamine and diisopropylethylamine.
- the alkyl radicals may, for example, also carry hydroxyl groups, as in the case of the dialkylmonoalkanol, alkyldialkanol and trialkanolamines.
- inorganic bases such as ammonia or sodium or potassium hydroxide may also be used as neutralizing agents. Preference is given to triethylamine, triethanolamine, dimethylethanolamine or diisopropylethylamine.
- the molar amount of the bases is between 50 and 100%, preferably between 70 and 100% of the molar amount of the anionic groups.
- cationic groups sulfuric acid dimethyl ester or succinic acid are used. If only nonionically hydrophilized compounds A.6) with ether groups are used, the neutralization step is omitted. The neutralization can also take place simultaneously with the dispersion in which the dispersing water already contains the neutralizing agent.
- This chain extension / termination can be carried out either in a solvent before dispersing, during dispersion or in water after dispersion.
- the chain extension is preferably carried out in water before dispersion.
- the chain extension of the prepolymers preferably takes place before the dispersion.
- the chain extension ie the equivalent ratio of NCO-reactive groups of the compounds used for chain extension to free NCO groups of the prepolymer is between 40 to 150%, preferably between 70 to 120%, particularly preferably between 80 to 120%.
- the aminic components [A.3), A.4), A.5)] can optionally be used individually or in mixtures in water- or solvent-diluted form in the process according to the invention, wherein basically any order of addition is possible.
- the diluent content is preferably 70 to 95% by weight.
- the preparation of the PU dispersion (I) from the prepolymers takes place after the chain extension.
- the dissolved and chain extended polyurethane polymer is optionally sheared under high shear, e.g. vigorous stirring, either added to the dispersing water or, conversely, the dispersing water is stirred into the prepolymer solutions.
- the water is added to the dissolved prepolymer.
- the solvent still present in the dispersions after the dispersion step is then usually removed by distillation. A removal already during the dispersion is also possible.
- the dispersion can be adjusted very finely divided, so that it has practically the appearance of a solution, but also very coarse-particle settings are possible, which are also sufficiently stable.
- the solids content of the PU dispersion (I) is between 25 to 65%, preferably 30 to 60% and particularly preferably between 40 to 60%.
- the ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) contain 5 to 45 wt .-% of component A.1), 50 to 94.5 wt .-% of components A.2), 0 to 15 wt .-% component A.3), 0.5 to 12 wt .-% component A.5), 0 to 15 wt .-% component A.6) wherein the sum of all components added to 100 wt .-%.
- the ionically modified hydroxyl-containing polyurethanes and / or polyurethane ureas (II) preferably contain 7.5 to 35% by weight of component A.1), 60 to 90% by weight of components A.2a), 0 to 10% by weight. Components A.3), 2.5 to 7.5 wt .-% component A.5), 0 to 12.5 wt .-% component A.6) wherein the sum of all components added to 100 wt .-%.
- the ionically modified hydroxyl-containing polyurethanes and / or polyurethane ureas (II) contain from 10 to 25% by weight of component II.1), 65 to 85 % By weight of components A.2), 1.5 to 5% by weight of component A.3), 3 to 7% by weight of component A.5), 0 to 10% by weight of component A.6) wherein the sum of all components added to 100 wt .-%.
- component A.3 only those compounds are suitable which are OH-functional.
- Components A.4) are not used to build up the polymers (II).
- the ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) preferably have a pure ionic hydrophilization according to the definition of components A.5).
- the coating compositions according to the invention contain the ionically modified, hydroxyl-containing polyurethanes and / or polyurethaneureas (II), which are either converted into the aqueous form during production and thus present as a dispersion or alternatively also in a, optionally water-miscible and isocyanate-inert solvent Solution available.
- the ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) can be prepared by the usual methods known in the art.
- the polyurethanes and / or polyurethane ureas (II) differ from the PUR polymers (I) in particular by the nature of the preparation and the type of hydrophilization. They contain carboxylic acid and / or sulfonic acid groups, preferably carboxylic acid groups, which may be at least partially neutralized, as hydrophilic groups.
- carboxylic acid and / or sulfonic acid groups preferably carboxylic acid groups, which may be at least partially neutralized, as hydrophilic groups.
- component A.5 those which have carboxy and / or carboxylate groups.
- Particularly preferred ionic compounds A.5) are dihydroxycarboxylic acids, very particularly preferred are ⁇ , ⁇ -dimethylolalkanoic acids, e.g. 2,2-dimethylolpropionic acid, 2,2-dimethylolbutyric acid or dihydroxysuccinic acid.
- hydroxyl-containing polyurethanes and / or polyurethane ureas are usually the components A.2), A.3), A.5) and optionally A.6), optionally together with a suitable catalyst and if necessary in presented a suitable solvent.
- a polyisocyanate A.1 is added and allowed to react until the reaction product is isocyanate.
- the amounts used of components A.1) to A.6) are so dimensioned that per val hydroxyl groups 0.45 to 0.95, preferably 0.55 to 0.90, particularly preferably 0.65 to 0.85 Val isocyanate groups come.
- the preparation of the ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) without addition of organic solvents is preferred.
- the acid groups incorporated in the prepolymer are at least partially neutralized. This can be done during or after the prepolymer but also during or after the dispersion in water by adding suitable neutralizing agent (see also in PU dispersion (I)).
- suitable neutralizing agents are triethylamine, triethanolamine, dimethylethanolamine, ethyldiisopropylamine or diisopropylethylamine.
- the neutralizing agent is usually used in molar ratio to the acid groups of the prepolymer of 0.3: 1 to 1.3: 1, preferably from 0.6: 1 to 1.1: 1.
- the hydroxyl-functional polyurethane is converted by the addition of water or by adding in water in an aqueous dispersion.
- the resins of the polyurethane polymers (II) obtainable by the procedure described above have a number-average molecular weight M n of from 1,000 to 30,000 Da, preferably from 1,500 to 10,000 Da, an acid number of from 10 to 80, preferably from 15 to 40 mg KOH / g and a hydroxyl group content of 0.5 to 6 wt .-%, preferably from 1.0 to 4 wt .-%.
- the PU dispersions (I) and (II) may additionally contain all additives known for PU dispersions, such as, for example, antioxidants, light stabilizers and / or other auxiliaries and additives as well as fillers.
- Crosslinkers (III) are also present in the coating compositions according to the invention.
- both one-component and two-component coatings can be prepared.
- one-component paints are to be understood as coating agents in which binder component and crosslinker component can be stored together, without a crosslinking reaction taking place in appreciable or detrimental extent for the subsequent application.
- Two-component coatings in the context of the present invention are understood to mean coating compositions in which binder component and crosslinker component must be stored in separate vessels because of their high reactivity. The two components are mixed just before application and then generally react without additional activation.
- Suitable crosslinkers III include, for example, blocked or unblocked polyisocyanate crosslinkers, amide and amine-formaldehyde resins, phenolic resins, aldehyde and ketone resins, e.g. Phenol-formaldehyde resins, resoles, furan resins, urea resins, carbamic acid ester resins, triazine resins, melamine resins, benzoguanamine resins, cyanamide resins or aniline resins. Preference is given to polyisocyanates.
- crosslinker component (III) Polyisocyanates with free isocyanate groups are particularly preferably used as crosslinker component (III), since the resulting aqueous polyurethane coatings show a particularly high paint-technical level.
- Suitable crosslinkers (III) are, for example, paint polyisocyanates such as uretdione, biuret, isocyanurate or iminooxadiazinedione polyisocyanates of hexamethylene diisocyanate, 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane or bis (4-isocyanatocyclohexane) methane.
- a two-component coating comprising the coating compositions according to the invention.
- PUR polymers (I) and (II) described here are generally sufficiently hydrophilic so that the dispersibility of hydrophobic crosslinkers of component (III) is ensured. If desired, however, it is also possible to add additional external emulsifiers as are known to the person skilled in the art.
- water-soluble or dispersible polyisocyanates as described, for example, in US Pat. obtainable by modification with carboxylate, sulfonate and / or polyethylene oxide groups and / or polyethylene oxide / polypropylene oxide groups are used in component (III).
- a process for preparing the aqueous coating compositions according to the invention characterized in that the PU polymers (I) and the PU polymers (II) are dispersed in water and mixed with the crosslinker (III).
- the ratio of the crosslinker (III) to the compounds of the components (II) which are reactive with it should be selected such that a ratio of crosslinker-reactive groups from (II) (eg OH groups) to the reactive groups of the crosslinker (at Isocyanate NCO groups) of 0.5: 1.0 to 3.5: 1.0, preferably 1.0: 1.0 to 3.0: 1.0, and more preferably 1.0: 1.0 to 2.5: 1.0 results.
- the mixture of components (I) and (II) contains preferably from 5 to 95% by weight (with respect to solid resin), more preferably from 25 to 75% by weight (with respect to solid resin) of component (II), the amount of (I) is to be chosen so that the total amounts of (I) and (II) add up to 100 wt .-% (in terms of solid resin).
- the substances known to the person skilled in the art such as defoaming agents, thickeners, pigments, dispersants, matting agents, catalysts, anti-skinning agents, anti-settling agents and / or emulsifiers, as well as additives which enhance the desired soft-feel effect, may be present in the coating compositions of the invention be. It is irrelevant at what point in the production of these added to the coating compositions of the invention or incorporated into this.
- aqueous coating compositions according to the invention are suitable for all fields of use in which aqueous coating and coating systems with high surface finish requirements of the films are used, e.g. Coating of mineral building material surfaces, painting and sealing of wood and wood-based materials, coating of metallic surfaces (metal coating), coating and coating of asphalt or bitumen-containing coatings, varnishing and sealing of various plastic surfaces (plastic coating) as well as high-gloss coatings.
- a preferred use of the coating compositions according to the invention is the production of soft feel effect paints, which ensure good hydrolysis resistances with very good haptic properties.
- Such coating compositions are preferably used in the plastic coating or in the wood finish, wherein the curing usually takes place at temperatures between room temperature and 130 ° C.
- the two-component technology with non-blocked polyisocyanates as crosslinker allows the use of comparatively low curing temperatures in o.g. Interval.
- aqueous coating compositions of the invention are usually used in single-coat paints or in the clearcoat or topcoat (top coat) of multi-layered structures.
- the preparation of the coating can be carried out by the different injection methods such as air pressure, airless or electrostatic spray method using single or optionally two-component spray systems.
- the lacquers and coating compositions containing the binder dispersions according to the invention can also be applied by other methods, for example by brushing, rolling or knife coating.
- the present invention likewise relates to a multilayer structure, characterized in that the topmost layer, which is a clear or topcoat layer, contains a softfeel lacquer containing the coating compositions according to the invention.
- the solids contents were determined according to DIN-EN ISO 3251.
- NCO contents were determined volumetrically in accordance with DIN-EN ISO 11909, unless expressly stated otherwise.
- a 151-reaction vessel with stirrer, heater and water with a condenser 1281 g of phthalic anhydride, 5058 g of adipic acid, 6387 g of 1,6-hexanediol and 675 g of neopentyl glycol were weighed and heated to 140 ° C under nitrogen in one hour. In a further 9 hours was heated to 220 ° C and condensed at this temperature until an acid number less than 3 was reached.
- the polyesterpolyol thus obtained had a viscosity (determined as the flow time of an 80% strength solution of the polyester in methoxypropyl acetate in the DIN 4 cup at 23 ° C.) of 54 seconds and an OH number of 160 mg KOH / g.
- 1,223 g of 1,4-butanediol and 535 g of 1,6-hexanediol were placed in a flask and heated to 100 ° C. Finally, about 2 1 / h nitrogen were introduced into the diol and 20 mbar vacuum applied and the mixture as long dehydrated (about 2 hours) until the water content was ⁇ 0.1%.
- the reaction mixture was cooled to 130 ° C and the pressure was lowered to 10 mbar. This was followed by an increase in the oil bath temperature from 130 ° C to 180 ° C within 2 h, the distillation head temperature did not exceed 60 ° C. After reaching 180 ° C, this temperature was maintained for 6 h.
- reaction mixture was cooled to 130 ° C and the pressure was lowered to 10 mbar. This was followed by an increase in the oil bath temperature from 130 ° C to 180 ° C within 2 h, the distillation head temperature did not exceed 60 ° C. After reaching 180 ° C, this temperature was maintained for 6 h. The reaction mixture was cooled to room temperature and the characteristics of the product determined.
- a polycarbonate diol having a hydroxyl number of 57.3 mg KOH / g and a viscosity of 115 Pas at 23 ° C. is obtained.
- the reaction mixture was cooled to 130 ° C and the pressure was lowered to 10 mbar. This was followed by an increase in the oil bath temperature from 130 ° C to 180 ° C within 2 h, the distillation head temperature did not exceed 60 ° C. After reaching 180 ° C, this temperature was maintained for 6 h.
- reaction mixture was cooled to 130 ° C and the pressure was lowered to 10 mbar. This was followed by an increase in the oil bath temperature from 130 ° C to 180 ° C within 2 h, the distillation head temperature did not exceed 60 ° C. After reaching 180 ° C, this temperature was maintained for 6 h. Thereafter, the reaction mixture was cooled to room temperature and the characteristics of the product determined.
- Bayhydrol ® XP 2429 aliphatic hydroxy-functional polyester-polyurethane dispersion of the prior art produced by using a polycarbonate diol, which is based solely on 1,6-hexanediol as the diol component, having a solids content of 55% (Bayer AG, Leverkusen, DE)
- the polyurethane thus obtained was cooled to 90 ° -100 ° C, 47 g of dimethylethanolamine (degree of neutralization 60%) was added, homogenized for 15 minutes and dispersed with 2270 g of demineralized water.
- the polyurethane thus obtained was cooled to 90 ° -100 ° C, 39 g dimethylethanolamine (degree of neutralization 50%) was added, homogenized for 15 minutes with 2270 g of demineralized water.
- Examples 1-9 are used for the following performance tests for the production of softfeel coatings:
- the parent lacquer is prepared by predispersion by trituration over a laboratory shaker.
- the temperature of the material to be ground should not exceed 40 ° C.
- the paint system is set to a flow time of approx. 30 s (DIN ISO 2431, 5 mm nozzle) and conventionally sprayed onto Bayblend ® T 65.
- the dry film thickness is between 30 and 40 ⁇ m.
- the pencil hardening method is a test for determining the paint film hardness.
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Abstract
Description
Die Erfindung betrifft wässrige Beschichtungsmittel auf Basis von Polycarbonatpolyolen, ein Verfahren zu deren Herstellung und Verwendung als Softfeel-Lack.The invention relates to aqueous coating compositions based on polycarbonate polyols, a process for their preparation and use as a soft-feel coating.
Polyurethanpolyharnstoffdispersionen (PUR-Dispersionen) und wässrige Zubereitungen von PUR-Dispersionen sind bekannter Stand der Technik. Ein wichtiges Einsatzgebiet wässriger Zubereitungen ionisch modifizierter PUR-Dispersionen liegt im Bereich der Lackierung von Kunststoffteilen.Polyurethane-polyurea dispersions (PU dispersions) and aqueous formulations of PU dispersions are known in the art. An important field of application of aqueous preparations of ionically modified PU dispersions lies in the area of the coating of plastic parts.
Aufgrund ästhetischer und technischer Anforderungen werden Kunststoffteile üblicherweise lackiert, um den Kunststoff vor äußeren Einflüssen, wie Sonnenlicht, chemischer, thermischer und mechanischer Beanspruchung zu schützen, um bestimmte Farbtöne und Farbeffekte zu erzielen, um Fehlstellen der Kunststoffoberfläche zu überdecken oder um der Kunststoffoberfläche einen angenehmen Griff (Haptik) zu verleihen. Zur Verbesserung der haptischen Eigenschaften von Kunststoffteilen werden in den letzten Jahren vermehrt sogenannte Softfeel Lacke eingesetzt. "Softfeel-Effekt" im Sinne der vorliegenden Erfindung bezeichnet ein besonderes Griffempfinden (Haptik) der lackierten Oberfläche; diese Haptik lässt sich mit Begriffen wie samtig, weich, gummiartig, warm umschreiben. Dem Trend folgend Emissionen von Lösemitteln in die Umwelt zu vermeiden, haben sich in den letzten Jahren wässrige Softfeel-Lacke auf Basis der Polyurethanchemie durchgesetzt, wie sie beispielhaft in der
Die Aufgabe der vorliegenden Erfindung bestand daher in der Bereitstellung von Beschichtungsmitteln, die neben dem o.g. mechanischen und haptischen Eigenschaften, im Vergleich zu Beschichtungsmitteln des Stands der Technik, zu signifikant hydrolysestabileren Beschichtungen führen.The object of the present invention was therefore to provide coating compositions which, in addition to the o.g. mechanical and haptic properties, compared to prior art coating compositions, lead to significantly more hydrolysis-stable coatings.
Wie beispielsweise in der
Es wurde nun gefunden, dass wässrige Zweikomponenten(2K)-Beschichtungsmittel, die sowohl nichtfunktionelle PUR-Polymere auf Basis von speziellen Polycarbonatpolyolen und hydrophile, hydroxylgruppenhaltige PUR-Polymere auf Basis von speziellen Polycarbonatpolyolen enthalten, eine ausgezeichnete Hydrolysestabilität und gleichzeitig die gewünschten haptischen Eigenschaften zeigen.It has now been found that aqueous two-component (2K) coating compositions containing both non-functional PUR polymers based on specific polycarbonate polyols and hydrophilic, hydroxyl-containing PUR polymers based on specific polycarbonate polyols exhibit excellent hydrolytic stability and at the same time the desired haptic properties.
Gegenstand der vorliegenden Erfindung sind daher wässrige Beschichtungsmittel enthaltend
- I) hydroxylgruppenfreie Polyurethane und/oder Polyurethanharnstoffe,
- II) ionisch modifizierte, hydroxylgruppenhaltige Polyurethane und/oder Polyurethanharnstoffe sowie
- III) mindestens einen Vernetzer,
- I) hydroxyl-free polyurethanes and / or polyurethane ureas,
- II) ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas and
- III) at least one crosslinker,
Im Verfahren zur Herstellung der nichtfunktionellen PUR-Polymere (I) werden als Aufbaukomponenten ausgewählt aus der Gruppe der Komponenten
- A.1) Polyisocyanate,
- A.2) polymere Polyole mit einem zahlenmittleren Molekulargewicht von Mn 200 bis 8000 g/mol, die Polycarbonatpolyole enthalten, die mindestens zu 25 Gew.-% aus 1,4-Butandiol als Aufbaukomponente bestehen,
- A.3) niedermolekulare Verbindungen des Molgewichts Mn 62 bis 400 g/mol die in Summe über zwei oder mehr Hydroxyl- und/oder Aminogruppen verfügen,
- A.4) Verbindungen, die über eine Hydroxy- oder Aminogruppe verfügen,
- A.5) isocyanatreaktive, ionische oder potentiell ionische Verbindungen sowie
- A.6) isocyanatreaktive, nichtionische hydrophile Verbindungen eingesetzt.
- A.1) polyisocyanates,
- A.2) polymeric polyols having a number average molecular weight of Mn 200 to 8000 g / mol, which contain polycarbonate polyols which consist of at least 25 wt .-% of 1,4-butanediol as a synthesis component,
- A.3) low molecular weight compounds of molecular weight Mn 62 to 400 g / mol which in total have two or more hydroxyl and / or amino groups,
- A.4) compounds which have a hydroxy or amino group,
- A.5) isocyanate-reactive, ionic or potentially ionic compounds as well
- A.6) isocyanate-reactive, nonionic hydrophilic compounds used.
Geeignete Polyisocyanate der Komponente A.1) sind die dem Fachmann an sich bekannten aromatischen, araliphatischen, aliphatischen oder cycloaliphatischen Polyisocyanate einer NCO-Funktionalität von bevorzugt ≥ 2, welche auch Iminooxadiazindion-, Isocyanurat-, Uretdion-, Urethan-, Allophanat-, Biuret-, Harnstoff-, Oxadiazintrion, Oxazolidinon-, Acylharnstoff- und/oder Carbodiimid-Strukturen aufweisen können. Diese können einzeln oder in beliebigen Mischungen untereinander eingesetzt werden.Suitable polyisocyanates of component A.1) are the aromatic, araliphatic, aliphatic or cycloaliphatic polyisocyanates of an NCO functionality known per se to the person skilled in the art of preferably ≥ 2, which may also have iminooxadiazinedione, isocyanurate, uretdione, urethane, allophanate, biuret, urea, oxadiazinetrione, oxazolidinone, acylurea and / or carbodiimide structures. These can be used individually or in any mixtures with each other.
Beispiele geeigneter Polyisocyanate sind Hexamethylendiisocyanat (HDI), Isophorondiisocyanat (IPDI), die isomeren Dicyclohexylmethan-4,4'-diisocyanat oder deren Mischungen beliebigen Isomerengehalts und 1,4-Cyclohexyldiisocyanat.Examples of suitable polyisocyanates are hexamethylene diisocyanate (HDI), isophorone diisocyanate (IPDI), the isomeric dicyclohexylmethane-4,4'-diisocyanate or mixtures thereof of any isomer content and 1,4-cyclohexyl diisocyanate.
Als Beispiel für ein nicht-modifiziertes Polyisocyanat mit mehr als 2 NCO-Gruppen pro Molekül sei z.B. 4-Isocyanatomethyl-1,8-octandiisocyanat (Nonantriisocyanat) genannt.As an example of a non-modified polyisocyanate having more than 2 NCO groups per molecule, see e.g. 4-Isocyanatomethyl-1,8-octane diisocyanate (nonane triisocyanate) called.
Bevorzugt handelt es sich um Polyisocyanate oder Polyisocyanatgemische der vorstehend genannten Art mit ausschließlich aliphatisch und/oder cycloaliphatisch gebundenen Isocyanatgruppen.Preference is given to polyisocyanates or polyisocyanate mixtures of the abovementioned type with exclusively aliphatically and / or cycloaliphatically bonded isocyanate groups.
Besonders bevorzugt sind Hexamethylendüsocyanat, Isophorondiisocyanat, die isomeren Dicyclohexylmethan-4,4'-diisocyanat sowie deren Mischungen.Particularly preferred are hexamethylene diisocyanate, isophorone diisocyanate, the isomeric dicyclohexylmethane-4,4'-diisocyanate and mixtures thereof.
Hydroxylgruppen aufweisende Polycarbonatpolyole entsprechend der Definition der Komponente A.2) sind durch Reaktion von Kohlensäurederivaten, z.B. Diphenylcarbonat, Dimethylcarbonat oder Phosgen mit Diolen erhältlich. Die erfindungsgemäß einzusetzenden hydroxyfunktionellen Polycarbonatpolyole A.2) haben eine mittlere Hydroxylfunktionalität von 1,6 bis 4, bevorzugt, 1,8 bis 3 und besonders bevorzugt 1,9 bis 2,3 und ein zahlenmittleres Molekulargewicht von 240 bis 8000 g/mol, bevorzugt von 500 bis 3000 g/mol, besonders bevorzugt von 750 bis 2500 g/mol. Die Herstellung der Polycarbonatpolyole erfolgt bevorzugt nach dem in der
Als Diole kommen z.B. 1,3- und 1,4-Butandiol, 1,6-Hexandiol, 1,8-Octandiol, 1,12-Dodecandiol, Neopentylglykol, 1,4-Bishydroxymethylcyclohexan, 2-Methyl-1,3-propandiol und Trimethylpentandiol-1,3 in Frage, wobei der Anteil an 1,4-Butandiol mindestens 25 Gew.-% der eingesetzten Diolkomponenten beträgt. Bevorzugt enthält die Diolkompomponente 45 bis 100 Gew.-% 1,4-Butandiol, und 0 bis 55 Gew.-% 1,6-Hexandiol, besonders bevorzugt 60 bis 100 Gew.-% 1,4-Butandiol und 0 bis 40 Gew.-% 1,6-Hexandiol.As diols come e.g. 1,3- and 1,4-butanediol, 1,6-hexanediol, 1,8-octanediol, 1,12-dodecanediol, neopentyl glycol, 1,4-bis-hydroxymethylcyclohexane, 2-methyl-1,3-propanediol and trimethylpentanediol-1 , 3 in question, wherein the proportion of 1,4-butanediol is at least 25 wt .-% of the diol components used. The diol component preferably contains 45 to 100% by weight 1,4-butanediol, and 0 to 55% by weight 1,6-hexanediol, particularly preferably 60 to 100% by weight 1,4-butanediol and 0 to 40% by weight .-% 1,6-hexanediol.
Die Hydroxylpolycarbonate sind bevorzugt linear, können jedoch gegebenenfalls durch den Einbau polyfunktioneller Komponenten, insbesondere niedermolekularer Polyole, verzweigt werden. Besonders bevorzugte Komponenten A.2) basieren auf Gemischen von 1,4-Butandiol und 1,6-Hexandiol und haben eine mittlere Hydroxylfunktionalität von 1,9 bis 2,05.The hydroxylpolycarbonates are preferably linear, but may optionally be branched by the incorporation of polyfunctional components, in particular low molecular weight polyols. Particularly preferred components A.2) are based on mixtures of 1,4-butanediol and 1,6-hexanediol and have an average hydroxyl functionality of 1.9 to 2.05.
Als polymere Polyole A.2) können ebenfalls beispielsweise Polyesterpolyole eingesetzt werden, die ein Molekulargewicht Mn von 400 bis 6000 Da, besonders bevorzugt von 600 bis 3000 Da aufweisen. Ihre Hydroxylzahl beträgt im Allgemeinen 22 bis 400 mg KOH/g, bevorzugt 50 bis 200 mg KOH/g und besonders bevorzugt 80 bis 160 mg KOH/g, und weisen eine OH-Funktionalität von 1,5 bis 6, bevorzugt von 1,8 bis 4 und besonders bevorzugt von 1,9 bis 3,3 auf.Polyester polyols which have a molecular weight Mn of from 400 to 6000 Da, more preferably from 600 to 3000 Da, can likewise be used as polymeric polyols A.2). Their hydroxyl number is generally 22 to 400 mg KOH / g, preferably 50 to 200 mg KOH / g and more preferably 80 to 160 mg KOH / g, and have an OH functionality of 1.5 to 6, preferably 1.8 to 4, and more preferably from 1.9 to 3.3.
Gut geeignete Beispiele sind die an sind die bekannten Polykondensate aus Di- sowie gegebenenfalls Polyolen und Di- sowie gegebenenfalls Polycarbonsäuren oder Hydroxycarbonsäuren oder Lactonen. Anstelle der freien Polycarbonsäuren können auch die entsprechenden Polycarbonsäureanhydride oder entsprechende Polycarbonsäureester von niederen Alkoholen zur Herstellung der Polyester verwendet werden. Beispiele für geeignete Diole sind Ethylenglykol, Butandiol(1,4), Hexandiol(1,6), Neopentylglykol Als gegebenenfalls mit einzusetzende Polyole sind hier beispielsweise Trimethylolpropan, Glycerin oder Pentaerythrit zu nennen.Highly suitable examples are the on are the known polycondensates of di- and optionally polyols and di- and optionally polycarboxylic acids or hydroxycarboxylic acids or lactones. Instead of the free polycarboxylic acids, it is also possible to use the corresponding polycarboxylic acid anhydrides or corresponding polycarboxylic acid esters of lower alcohols for the preparation of the polyesters. Examples of suitable diols are ethylene glycol, butanediol (1,4), hexanediol (1,6), neopentyl glycol. Examples of suitable polyols which may be used here are trimethylolpropane, glycerol or pentaerythritol.
Als Dicarbonsäuren kommen bevorzugt in Frage Phthalsäure, Isophthalsäure, Terephthalsäure, Tetrahydrophthalsäure, Hexahydrophthalsäure, oder Adipinsäure. Anhydride dieser Säuren sind ebenfalls geeignet, soweit sie existieren. Für die Belange der vorliegenden Erfindung werden die Anhydride infolgedessen durch den Ausdruck "Säure" umfasst. Es können auch Monocarbonsäuren, wie Benzoesäure und Hexancarbonsäure verwendet werden, vorausgesetzt, dass die mittlere Funktionalität des Polyols höher als 2 ist. Als gegebenenfalls in kleineren Mengen mitzuverwendende Polycarbonsäure sei hier Trimellitsäure genannt.Suitable dicarboxylic acids are preferably phthalic acid, isophthalic acid, terephthalic acid, tetrahydrophthalic acid, hexahydrophthalic acid, or adipic acid. Anhydrides of these acids are also suitable, as far as they exist. As a result, for the purposes of the present invention, the anhydrides are encompassed by the term "acid". Monocarboxylic acids such as benzoic acid and hexanecarboxylic acid can also be used, provided that the average functionality of the polyol is higher than 2. As polycarboxylic acid which may optionally be used in smaller amounts, trimellitic acid may be mentioned here.
Weitere geeignete Komponenten A.2) sind die aus der Polyurethanchemie bekannten Polylacton-und Polyetherpolyole soweit sie bezüglich Funktionalität und Molekulargewicht den oben genannten Kriterien entsprechen.Further suitable components A.2) are the polylactone and polyether polyols known from polyurethane chemistry, insofar as they correspond to the abovementioned criteria in terms of functionality and molecular weight.
Der Anteil der Hydroxylpolycarbonate an der Summe der eingesetzten Polyole aus A.2) zur Herstellung der Polymere (I) bzw. (II) beträgt 35 bis 100 Gew.-%, bevorzugt 45 bis 100 Gew.-% und besonders bevorzugt 65 bis 100 Gew.-%.The proportion of the hydroxyl polycarbonates in the sum of the polyols used from A.2) for the preparation of the polymers (I) or (II) is 35 to 100 wt .-%, preferably 45 to 100 wt .-% and particularly preferably 65 to 100 wt .-%.
Die zum Aufbau der Polyurethanharze eingesetzten niedermolekularen Polyole A.3) bewirken in der Regel eine Versteifung und oder eine Verzweigung der Polymerkette. Das Molekulargewicht liegt bevorzugt zwischen 62 und 200 Da. Geeignete Polyole können aliphatische, alicyclische oder aromatische Gruppen enthalten. Genannt seien hier beispielsweise die niedermolekularen Polyole mit bis zu etwa 20 Kohlenstoffatomen je Molekül, wie z. B. Ethylenglykol, Diethylenglykol, 1,4-Butandiol, 1,3-Butylenglykol, Cyclohexandiol, 1,4-Cyclohexandimethanol, 1,6-Hexandiol sowie Trimethylolpropan, Glycerin oder Pentaerythrit.The low molecular weight polyols A.3) used to build up the polyurethane resins generally cause stiffening and / or branching of the polymer chain. The molecular weight is preferably between 62 and 200 Da. Suitable polyols may contain aliphatic, alicyclic or aromatic groups. Mentioned here are, for example, the low molecular weight polyols having up to about 20 carbon atoms per molecule, such as. As ethylene glycol, diethylene glycol, 1,4-butanediol, 1,3-butylene glycol, cyclohexanediol, 1,4-cyclohexanedimethanol, 1,6-hexanediol and trimethylolpropane, glycerol or pentaerythritol.
Di- oder Polyamine sowie Hydrazide können ebenfalls als A.3) eingesetzt werden, z.B. Ethylendiamin, 1,2- und 1,3-Diaminopropan, 1,4-Diaminobutan, 1,6-Diaminohexan, Isophorondiamin, Isomerengemisch von 2,2,4- und 2,4,4-Trimethylhexamethylendiamin, 2-Methylpentamethylendiamin, Diethylentriamin, 1,3- und 1,4-Xylylendiamin, α,α,α',α'-Tetramethyl-1,3- und -1,4-xylylendiamin und 4,4-Diaminodicyclohexylmethan, Dimethylethylendiamin, Hydrazin oder Adipinsäuredihydrazid. Als A.3) kommen prinzipiell auch Verbindungen in Betracht, die aktiven Wasserstoff mit gegenüber NCO-Gruppen unterschiedlicher Reaktivität enthalten, wie Verbindungen, die neben einer primären Aminogruppe auch sekundäre Aminogruppen oder neben einer Aminogruppe (primär oder sekundär) auch OH-Gruppen aufweisen.Di- or polyamines as well as hydrazides can also be used as A.3), e.g. Ethylenediamine, 1,2- and 1,3-diaminopropane, 1,4-diaminobutane, 1,6-diaminohexane, isophoronediamine, isomer mixture of 2,2,4- and 2,4,4-trimethylhexamethylenediamine, 2-methylpentamethylenediamine, diethylenetriamine, 1,3- and 1,4-xylylenediamine, α, α, α ', α'-tetramethyl-1,3- and 1,4-diaminodicyclohexylmethane, dimethylethylenediamine, hydrazine or adipic dihydrazide. In principle, compounds which contain active hydrogen with respect to NCO groups of different reactivity, such as compounds which, in addition to a primary amino group, also have secondary amino groups or OH groups in addition to an amino group (primary or secondary), are also suitable as A.3).
Die Polyurethanharze I) und II) können auch gegebenenfalls Bausteine A.4) enthalten, die sich jeweils an den Kettenenden befinden und diese abschließen. Diese Bausteine leiten sich zum einen von monofunktionellen, mit NCO-Gruppen reaktiven Verbindungen ab, wie Monoaminen, insbesondere mono-sekundären Aminen oder Monoalkoholen.The polyurethane resins I) and II) may also contain, if appropriate, building blocks A.4), which are located in each case at the chain ends and terminate them. These building blocks are derived, on the one hand, from monofunctional compounds reactive with NCO groups, such as monoamines, in particular mono-secondary amines or monoalcohols.
Unter ionisch bzw. potentiell ionisch hydrophilierenden Verbindungen A.5) werden sämtliche Verbindungen verstanden, die mindestens eine isocyanatreaktive Gruppe sowie mindestens eine Funktionalität, wie z.B. -COOY, -SO3Y, -PO(OY)2 (Y beispielsweise = H, NH4 +, Metallkation), -NR2, -NR3 + (R = H, Alkyl, Aryl), aufweisen, die bei Wechselwirkung mit wässrigen Medien ein pH-Wert-abhängiges Dissoziationsgleichgewicht eingeht und auf diese Weise negativ, positiv oder neutral geladen sein kann. Bevorzugte isocyanatreaktive Gruppen sind Hydroxyl- oder Aminogruppen.By ionic or potentially ionic hydrophilizing compounds A.5) are meant all compounds which have at least one isocyanate-reactive group and at least one functionality such as -COOY, -SO 3 Y, -PO (OY) 2 (Y, for example = H, NH 4 + , metal cation), -NR 2 , -NR 3 + (R = H, alkyl, aryl), which undergo a pH-dependent dissociation equilibrium when interacting with aqueous media and in this way charge negative, positive or neutral can be. Preferred isocyanate-reactive groups are hydroxyl or amino groups.
Geeignete ionisch oder potentiell ionisch hydrophilierende Verbindungen entsprechend der Definition der Komponente A.5) sind z.B. Mono- und Dihydroxycarbonsäuren, Mono- und Diaminocarbonsäuren, Mono- und Dihydroxysulfonsäuren, Mono- und Diaminosulfonsäuren sowie Mono- und Dihydroxyphosphonsäuren oder Mono- und Diaminophosphonsäuren und ihre Salze wie Dimethylolpropionsäure, Dimethylolbuttersäure, Hydroxypivalinsäure, N-(2-Aminoethyl)-β-alanin, 2-(2-Amino-ethylamino)-ethansulfonsäure, Ethylendiamin-propyl- oder -butylsulfonsäure, 1,2- oder 1,3-Propylendiamin-β-ethylsulfonsäure, Äpfelsäure, Zitronensäure, Glykolsäure, Milchsäure, Glycin, Alanin, Taurin, Lysin, 3,5-Diaminobenzoesäure, ein Additionsprodukt von aliphatischen Diamninen wie z.B. Ethylendiamin (EDA) oder Isophorondiamin IPDA und Acrylsäure (
Zum Aufbau der Komponente I) sind solche Verbindungen A.5) bevorzugt, die über Carboxy- oder Carboxylat- und/oder Sulfonatgruppen und/oder Ammoniumgruppen verfügen. Besonders bevorzugte ionische Verbindungen A.5) sind solche, die Carboxyl- und/oder Sulfonatgruppen als ionische oder potentiell ionische Gruppen enthalten, wie die Salze von N-(2-Aminoethyl)-β-alanin, der 2-(2-Amino-ethylamino-)ethansulfonsäure oder des Additionsproduktes von IPDI und Acrylsäure (
Geeignete nichtionisch hydrophilierende Verbindungen entsprechend der Definition der Komponente A.6) sind z.B. Polyoxyalkylenether, die mindestens eine Hydroxy- oder Aminogruppe enthalten. Diese Polyether enthalten einen Anteil von 30 Gew.-% bis 100 Gew.-% an Bausteinen, die vom Ethylenoxid abgeleitet sind.Suitable nonionic hydrophilic compounds according to the definition of component A.6) are e.g. Polyoxyalkylene ethers containing at least one hydroxy or amino group. These polyethers contain from 30% to 100% by weight of building blocks derived from ethylene oxide.
Bei den Polyalkylenoxidpolyetheralkoholen handelt es sich entweder um reine Polyethylenoxidpolyether oder gemischte Polyalkylenoxidpolyether, deren Alkylenoxideinheiten zu mindestens 30 mol-%, bevorzugt zu mindestens 40 mol-% aus Ethylenoxideinheiten bestehen. Bevorzugte nichtionische Verbindungen sind monofunktionelle gemischte Polyalkylenoxidpolyether, die mindestens 40 mol-% Ethylenoxid- und maximal 60 mol% Propylenoxideinheiten aufweisen.The polyalkylene oxide polyether alcohols are either pure polyethylene oxide polyethers or mixed polyalkylene oxide polyethers whose alkylene oxide units consist of at least 30 mol%, preferably at least 40 mol%, of ethylene oxide units. Preferred nonionic compounds are monofunctional mixed polyalkylene oxide polyethers which have at least 40 mol% of ethylene oxide and not more than 60 mol% of propylene oxide units.
Für die PUR-Polymere (I) werden bevorzugt eine Kombination aus ionischen und nicht-ionischen Hydrophilierungsmitteln entsprechend den Definitionen der Komponenten A.5) und A.6) verwendet. Besonders bevorzugt sind Kombinationen aus nichtionischen und anionischen Hydrophilierungsmitteln.For the PUR polymers (I) it is preferred to use a combination of ionic and nonionic hydrophilicizing agents according to the definitions of components A.5) and A.6). Particularly preferred are combinations of nonionic and anionic hydrophilicizing agents.
Bevorzugt werden 5 bis 45 Gew.-% Komponente A.1), 50 bis 90 Gew.-% Komponente A.2), 1 bis 30 Gew.-% der Summe von Verbindungen A.3) und A.4), 0 bis 12 Gew.-% Komponente A.5), 0 bis 15 Gew.-% Komponente A.6) eingesetzt, wobei die Summe von A.5) und A.6) 0,1 bis 27 Gew.-% beträgt und sich die Summe aller Komponenten zu 100 Gew.-% addiert.Preference is given to 5 to 45 wt .-% of component A.1), 50 to 90 wt .-% of component A.2), 1 to 30 wt .-% of the sum of compounds A.3) and A.4), 0 from 0 to 15% by weight of component A6), the sum of A.5) and A.6) being from 0.1 to 27% by weight, and the sum of all components added to 100 wt .-%.
Besonders bevorzugt werden 10 bis 40 Gew.-% Komponente A.1), 55 bis 85 Gew.-% Komponente A.2), 1 bis 25 Gew.-% der Summe von Verbindungen A.3) und A.4), 0 bis 10 Gew.-% Komponente A.5), 0 bis 10 Gew.-% Komponente A.6) eingesetzt, wobei die Summe von A.5) und A.6) 0,1 bis 20 Gew.-% beträgt und sich die Summe aller Komponenten zu 100 Gew.-% addiert.10 to 40% by weight of component A.1), 55 to 85% by weight of component A.2), 1 to 25% by weight of the sum of compounds A.3) and A.4) are particularly preferred, 0 to 10% by weight of component A.5), 0 to 10% by weight of component A.6), the sum of A.5) and A.6) being 0.1 to 20% by weight and the sum of all components added to 100 wt .-%.
Ganz besonders bevorzugt werden 15 bis 40 Gew.-% Komponente A.1), 60 bis 85 Gew.-% Komponente A.2), 1 bis 20 Gew.-% der Summe von Verbindungen A.3), 0 bis 8 Gew.-% Komponente A.5), 0 bis 10 Gew.-% Komponente A.6) eingesetzt, wobei die Summe von A.5) und A.6) 0,1 bis 18 Gew.-% beträgt und sich die Summe aller Komponenten zu 100 Gew.-% addiert.Very particular preference is given to 15 to 40% by weight of component A.1), 60 to 85% by weight of component A.2), 1 to 20% by weight of the sum of compounds A.3), 0 to 8% by weight .-% Component A.5), 0 to 10 wt .-% component A.6) used, wherein the sum of A.5) and A.6) is 0.1 to 18 wt .-% and the sum of all components to 100 wt .-% added.
Die erfindungsgemäßen Beschichtungsmittel enthalten PUR-Polymere (I), die in Form ihrer wässrigen PUR-Dispersion (I) eingesetzt werden.The coating compositions according to the invention comprise PU polymers (I) which are used in the form of their aqueous PU dispersion (I).
Das Verfahren zur Herstellung der wässrigen PUR-Dispersion (I) kann in einer oder mehreren Stufen in homogener oder bei mehrstufiger Umsetzung, teilweise in disperser Phase durchgeführt werden. Nach vollständig oder teilweise durchgeführter Polyaddition aus A.1) - A.6) erfolgt ein Dispergier-, Emulgier- oder Lösungsschritt. Im Anschluss erfolgt gegebenenfalls eine weitere Polyaddition oder Modifikation in disperser Phase.The process for the preparation of the aqueous PU dispersion (I) can be carried out in one or more stages in homogeneous or in multistage reaction, partly in disperse phase. After completely or partially carried out polyaddition from A.1) - A.6) takes place a dispersing, emulsifying or dissolving step. This is followed, if appropriate, by a further polyaddition or modification in disperse phase.
Zur Herstellung der wässrigen PUR-Dispersionen (I) können alle aus dem Stand der Technik bekannten Verfahren wie z. B. Prepolymer-Mischverfahren, Acetonverfahren oder Schmelzdipergierverfahren verwendet werden. Bevorzugt wird die PUR-Dispersion (I) nach dem Aceton-Verfahren hergestellt.For the preparation of the aqueous polyurethane dispersions (I), all known from the prior art methods such as. Example, prepolymer mixing method, acetone method or Schmelzdipergierverfahren can be used. The PU dispersion (I) is preferably prepared by the acetone process.
Für die Herstellung der PUR-Dispersion (I) nach dem Aceton-Verfahren werden üblicherweise die Bestandteile A.2) bis A.6), die keine primären oder sekundären Aminogruppen aufweisen dürfen und die Polyisocyanatkomponente A.1) zur Herstellung eines isocyanatfunktionellen Polyurethan-Prepolymers ganz oder teilweise vorgelegt und gegebenenfalls mit einem mit Wasser mischbaren aber gegenüber Isocyanatgruppen inerten Lösungsmittel verdünnt und auf Temperaturen im Bereich von 50 bis 120°C aufgeheizt. Zur Beschleunigung der Isocyanatadditionsreaktion können die in der Polyurethan-Chemie bekannten Katalysatoren eingesetzt werden. Bevorzugt ist Dibutylzinndilaurat.For the preparation of the PU dispersion (I) by the acetone process are usually the components A.2) to A.6), which may have no primary or secondary amino groups and the polyisocyanate component A.1) for the preparation of an isocyanate-functional polyurethane Prepolymer presented in whole or in part and optionally diluted with a water-miscible but isocyanate-inert solvent and heated to temperatures ranging from 50 to 120 ° C. To accelerate the isocyanate addition reaction, the catalysts known in polyurethane chemistry can be used. Preference is given to dibutyltin dilaurate.
Geeignete Lösungsmittel sind die üblichen aliphatischen, ketofunktionellen Lösemittel wie z.B. Aceton, Butanon, die nicht nur zu Beginn der Herstellung, sondern gegebenenfalls in Teilen auch später zugegeben werden können. Bevorzugt sind Aceton und Butanon.Suitable solvents are the usual aliphatic, ketofunctional solvents, e.g. Acetone, butanone, which can be added not only at the beginning of the preparation, but possibly also in parts later. Preferred are acetone and butanone.
Anschließend werden die gegebenenfalls zu Beginn der Reaktion noch nicht zugegebenen Bestandteile von A.1) ― A.6) zudosiert.Subsequently, the components of A.1) - A.6) which may not have been added at the beginning of the reaction are subsequently metered in.
Bei der Herstellung des Polyurethan-Prepolymeren beträgt das Stoffmengenverhältnis von Isocyanatgruppen zu mit Isocyanat reaktiven Gruppen 1,0 bis 3,5, bevorzugt 1,1 bis 3,0, besonders bevorzugt 1,1 bis 2,5.In the preparation of the polyurethane prepolymer, the molar ratio of isocyanate groups to isocyanate-reactive groups is 1.0 to 3.5, preferably 1.1 to 3.0, particularly preferably 1.1 to 2.5.
Die Umsetzung der Komponenten A.1) - A.6) zum Prepolymer erfolgt teilweise oder vollständig, bevorzugt aber vollständig. Es werden so Polyurethan-Prepolymere, die freie Isocyanatgruppen enthalten, in Substanz oder in Lösung erhalten.The reaction of the components A.1) - A.6) to the prepolymer takes place partially or completely, but preferably completely. Thus, polyurethane prepolymers containing free isocyanate groups are obtained in bulk or in solution.
Nach oder während der Herstellung der Polyurethan-Prepolymere erfolgt, falls dies noch nicht in den Ausgangsmolekülen durchgeführt wurde, die teilweise oder vollständige Salzbildung der anionisch und/oder kationisch dispergierend wirkenden Gruppen. Im Falle anionischer Gruppen werden dazu Basen wie tertiäre Amine, z.B. Trialkylamine mit 1 bis 12, bevorzugt 1 bis 6 C-Atomen in jedem Alkylrest eingesetzt. Beispiele hierfür sind Trimethylamin, Triethylamin, Methyldiethylamin, Tripropylamin und Diisopropylethylamin. Die Alkylreste können beispielsweise auch Hydroxylgruppen tragen, wie bei den Dialkylmonoalkanol-, Alkyldialkanol- und Trialkanolaminen. Als Neutralisationsmittel sind gegebenenfalls auch anorganische Basen, wie Ammoniak oder Natrium- bzw. Kaliumhydroxid einsetzbar. Bevorzugt sind Triethylamin, Triethanolamin, Dimethylethanolamin oder Diisopropylethylamin.After or during the preparation of the polyurethane prepolymers, if this has not yet been carried out in the starting molecules, the partial or complete salt formation of the anionically and / or cationically dispersing groups takes place. In the case of anionic groups, bases such as tertiary amines, e.g. Trialkylamines having 1 to 12, preferably 1 to 6 carbon atoms used in each alkyl radical. Examples of these are trimethylamine, triethylamine, methyldiethylamine, tripropylamine and diisopropylethylamine. The alkyl radicals may, for example, also carry hydroxyl groups, as in the case of the dialkylmonoalkanol, alkyldialkanol and trialkanolamines. If appropriate, inorganic bases such as ammonia or sodium or potassium hydroxide may also be used as neutralizing agents. Preference is given to triethylamine, triethanolamine, dimethylethanolamine or diisopropylethylamine.
Die Stoffmenge der Basen liegt zwischen 50 und 100 %, bevorzugt zwischen 70 und 100 % der Stoffmenge der anionischen Gruppen. Im Falle kationischer Gruppen werden Schwefelsäuredimethylester oder Bernsteinsäure eingesetzt. Werden nur nichtionisch hydrophilierte Verbindungen A.6) mit Ethergruppen verwendet, entfällt der Neutralisationsschritt. Die Neutralisation kann auch gleichzeitig mit der Dispergierung erfolgen, in dem das Dispergierwasser bereits das Neutralisationsmittel enthält.The molar amount of the bases is between 50 and 100%, preferably between 70 and 100% of the molar amount of the anionic groups. In the case of cationic groups, sulfuric acid dimethyl ester or succinic acid are used. If only nonionically hydrophilized compounds A.6) with ether groups are used, the neutralization step is omitted. The neutralization can also take place simultaneously with the dispersion in which the dispersing water already contains the neutralizing agent.
Im Anschluss wird in einem weiteren Verfahrensschritt, falls noch nicht oder nur teilweise geschehen das erhaltene Prepolymer mit Hilfe von aliphatischen Ketonen wie Aceton oder Butanon gelöst.Subsequently, in a further process step, if not yet done or only partially done, the resulting prepolymer with the aid of aliphatic ketones such as acetone or butanone.
Anschließend werden mögliche NH2- und/oder NH-funktionelle Komponenten mit den noch verbliebenen Isocyanatgruppen umgesetzt. Diese Kettenverlängerung/-terminierung kann dabei entweder in Lösungsmittel vor dem Dispergieren, während des Dispergierens oder in Wasser nach dem Dispergieren durchgeführt werden. Bevorzugt wird die Kettenverlängerung vor der Dispergierung in Wasser durchgeführt.Subsequently, possible NH 2 - and / or NH-functional components are reacted with the remaining isocyanate groups. This chain extension / termination can be carried out either in a solvent before dispersing, during dispersion or in water after dispersion. The chain extension is preferably carried out in water before dispersion.
Werden zur Kettenverlängerung Verbindungen entsprechend der Definition von A.5) mit NH2-oder NH-Gruppen eingesetzt, erfolgt die Kettenverlängerung der Prepolymere bevorzugt vor der Dispergierung.If compounds corresponding to the definition of A.5) with NH 2 or NH groups are used for chain extension, the chain extension of the prepolymers preferably takes place before the dispersion.
Der Kettenverlängerungsgrad, also das Äquivalentverhältnis von NCO-reaktiven Gruppen der zur Kettenverlängerung eingesetzten Verbindungen zu freien NCO-Gruppen des Prepolymers liegt zwischen 40 bis 150 %, bevorzugt zwischen 70 bis 120 %, besonders bevorzugt zwischen 80 bis 120%.The chain extension, ie the equivalent ratio of NCO-reactive groups of the compounds used for chain extension to free NCO groups of the prepolymer is between 40 to 150%, preferably between 70 to 120%, particularly preferably between 80 to 120%.
Die aminischen Komponenten [A.3), A.4), A.5)] können gegebenenfalls in wasser- oder lösemittelverdünnter Form im erfindungsgemäßen Verfahren einzeln oder in Mischungen eingesetzt werden, wobei grundsätzlich jede Reihenfolge der Zugabe möglich ist.The aminic components [A.3), A.4), A.5)] can optionally be used individually or in mixtures in water- or solvent-diluted form in the process according to the invention, wherein basically any order of addition is possible.
Wenn Wasser oder organische Lösemittel als Verdünnungsmittel mitverwendet werden so beträgt der Verdünnungsmittelgehalt bevorzugt 70 bis 95 Gew.-%.If water or organic solvents are used as diluents, the diluent content is preferably 70 to 95% by weight.
Die Herstellung der PUR-Dispersion (I) aus den Prepolymeren erfolgt im Anschluss an die Kettenverlängerung. Dazu wird das gelöste und kettenverlängerte Polyurethanpolymer gegebenenfalls unter starker Scherung, wie z.B. starkem Rühren, entweder in das Dispergierwasser eingetragen oder es wird umgekehrt das Dispergierwasser zu den Prepolymerlösungen gerührt. Bevorzugt wird das Wasser in das gelöste Prepolymer gegeben.The preparation of the PU dispersion (I) from the prepolymers takes place after the chain extension. To this end, the dissolved and chain extended polyurethane polymer is optionally sheared under high shear, e.g. vigorous stirring, either added to the dispersing water or, conversely, the dispersing water is stirred into the prepolymer solutions. Preferably, the water is added to the dissolved prepolymer.
Das in den Dispersionen nach dem Dispergierschritt noch enthaltene Lösemittel wird üblicherweise anschließend destillativ entfernt. Eine Entfernung bereits während der Dispergierung ist ebenfalls möglich.The solvent still present in the dispersions after the dispersion step is then usually removed by distillation. A removal already during the dispersion is also possible.
Je nach Neutralisationsgrad und Gehalt ionischer Gruppen kann die Dispersion sehr feinteilig eingestellt werden, so dass sie praktisch das Aussehen einer Lösung hat, aber auch sehr grobteilige Einstellungen sind möglich, die ebenfalls ausreichend stabil sind.Depending on the degree of neutralization and content of ionic groups, the dispersion can be adjusted very finely divided, so that it has practically the appearance of a solution, but also very coarse-particle settings are possible, which are also sufficiently stable.
Der Feststoffgehalt der PUR-Dispersion (I) liegt zwischen 25 bis 65 %, bevorzugt 30 bis 60 % und besonders bevorzugt zwischen 40 bis 60 %.The solids content of the PU dispersion (I) is between 25 to 65%, preferably 30 to 60% and particularly preferably between 40 to 60%.
Die ionisch modifizierten, hydroxylgruppenhaltigen Polyurethane und/oder Polyurethanharnstoffe (II) enthalten 5 bis 45 Gew.-% Komponente A.1), 50 bis 94,5 Gew.-% Komponenten A.2), 0 bis 15 Gew.-% Komponente A.3), 0,5 bis 12 Gew.-% Komponente A.5), 0 bis 15 Gew.-% Komponente A.6) wobei die Summe aller Komponenten zu 100 Gew.-% addiert.The ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) contain 5 to 45 wt .-% of component A.1), 50 to 94.5 wt .-% of components A.2), 0 to 15 wt .-% component A.3), 0.5 to 12 wt .-% component A.5), 0 to 15 wt .-% component A.6) wherein the sum of all components added to 100 wt .-%.
Bevorzugt enthalten die ionisch modifizierten, hydroxylgruppenhaltigen Polyurethane und/oder Polyurethanharnstoffe (II) 7,5 bis 35 Gew.-% Komponente A.1), 60 bis 90 Gew.-% Komponenten A.2a), 0 bis 10 Gew.-% Komponenten A.3), 2,5 bis 7,5 Gew.-% Komponente A.5), 0 bis 12,5 Gew.-% Komponente A.6) wobei die Summe aller Komponenten zu 100 Gew.-% addiert.The ionically modified hydroxyl-containing polyurethanes and / or polyurethane ureas (II) preferably contain 7.5 to 35% by weight of component A.1), 60 to 90% by weight of components A.2a), 0 to 10% by weight. Components A.3), 2.5 to 7.5 wt .-% component A.5), 0 to 12.5 wt .-% component A.6) wherein the sum of all components added to 100 wt .-%.
Ganz besonders bevorzugt enthalten die ionisch modifizierten, hydroxylgruppenhaltigen Polyurethane und/oder Polyurethanharnstoffe (II) 10 bis 25 Gew.-% Komponente II.1), 65 bis 85 Gew.-% Komponenten A.2), 1,5 bis 5 Gew.-% Komponente A.3), 3 bis 7 Gew.-% Komponente A.5), 0 bis 10 Gew.-% Komponente A.6) wobei die Summe aller Komponenten zu 100 Gew.-% addiert.Most preferably, the ionically modified hydroxyl-containing polyurethanes and / or polyurethane ureas (II) contain from 10 to 25% by weight of component II.1), 65 to 85 % By weight of components A.2), 1.5 to 5% by weight of component A.3), 3 to 7% by weight of component A.5), 0 to 10% by weight of component A.6) wherein the sum of all components added to 100 wt .-%.
Als Komponenten- A.3) kommen nur solche Verbindungen in Frage, die OH-funktionell sind. Komponenten A.4) werden zum Aufbau der Polymere (II) nicht eingesetzt.As component A.3), only those compounds are suitable which are OH-functional. Components A.4) are not used to build up the polymers (II).
Die ionisch modifizierten, hydroxylgruppenhaltigen Polyurethane und/oder Polyurethanharnstoffe (II) weisen bevorzugt eine reine ionische Hydrophilierung entsprechend der Definition der Komponenten A.5) auf. Die erfindungsgemäßen Beschichtungsmittel enthalten die ionisch modifizierten, hydroxylgruppenhaltigen Polyurethane und/oder Polyurethanharnstoffe (II), die bei der Herstellung entweder in die wässrige Form überführt werden und somit als Dispersion vorliegen oder alternativ auch in einem, gegebenenfalls mit Wasser mischbaren und gegenüber Isocyanatgruppen inerten Lösungsmittel als Lösung vorliegen.The ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) preferably have a pure ionic hydrophilization according to the definition of components A.5). The coating compositions according to the invention contain the ionically modified, hydroxyl-containing polyurethanes and / or polyurethaneureas (II), which are either converted into the aqueous form during production and thus present as a dispersion or alternatively also in a, optionally water-miscible and isocyanate-inert solvent Solution available.
Die ionisch modifizierten, hydroxylgruppenhaltigen Polyurethane und/oder Polyurethanharnstoffe (II) können nach den üblichen, im Stand der Technik bekannten Verfahren hergestellt werden. Die Polyurethane und/oder Polyurethanharnstoffe (II) unterscheiden sich von den PUR-Polymeren (I) insbesondere durch die Art der Herstellung und der Art der Hydrophilierung. Sie enthalten Carbonsäure- und/oder Sulfonsäuregruppen, bevorzugt Carbonsäuregruppen, die zumindest anteilig neutralisiert sein können, als hydrophile Gruppen. Zur Herstellung der PUR-Polymere (II) werden daher als Komponente A.5) solche bevorzugt, die über Carboxy- und/oder Carboxylatgruppen verfügen. Besonders bevorzugte ionische Verbindungen A.5) sind Dihydroxycarbonsäuren, ganz besonders bevorzugt sind α,α-Dimethylolalkansäuren, wie z.B. 2,2-Dimethylolpropionsäure, 2,2-Dimethylolbuttersäure oder Dihydroxybernsteinsäure.The ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) can be prepared by the usual methods known in the art. The polyurethanes and / or polyurethane ureas (II) differ from the PUR polymers (I) in particular by the nature of the preparation and the type of hydrophilization. They contain carboxylic acid and / or sulfonic acid groups, preferably carboxylic acid groups, which may be at least partially neutralized, as hydrophilic groups. For the preparation of the PUR polymers (II) are therefore preferred as component A.5) those which have carboxy and / or carboxylate groups. Particularly preferred ionic compounds A.5) are dihydroxycarboxylic acids, very particularly preferred are α, α-dimethylolalkanoic acids, e.g. 2,2-dimethylolpropionic acid, 2,2-dimethylolbutyric acid or dihydroxysuccinic acid.
Zur Herstellung der ionisch modifizierten, hydroxylgruppenhaltigen Polyurethane und/oder Polyurethanharnstoffe (II) werden üblicherweise die Komponenten A.2), A.3), A.5) und gegebenenfalls A.6), gegebenenfalls zusammen mit einem geeigneten Katalysator und bei Bedarf in einem geeigneten Lösemittel vorgelegt. In diese Mischung wird bei einer Temperatur von 0 bis 140°C, bevorzugt 70 bis 135°C und besonders bevorzugt bei 90 bis 130°C eine Polyisocyanatkomponente A.1) zugegeben und reagieren gelassen, bis das Reaktionsprodukt isocyanatfrei ist. Dabei werden die Einsatzmengen der Komponenten A.1) bis A.6) so bemessen, dass pro Val Hydroxylgruppen 0,45 bis 0,95, bevorzugt 0,55 bis 0,90, besonders bevorzugt 0,65 bis 0,85 Val Isocyanatgruppen kommen.For the preparation of the ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) are usually the components A.2), A.3), A.5) and optionally A.6), optionally together with a suitable catalyst and if necessary in presented a suitable solvent. In this mixture, at a temperature of 0 to 140 ° C, preferably 70 to 135 ° C and more preferably at 90 to 130 ° C, a polyisocyanate A.1) is added and allowed to react until the reaction product is isocyanate. The amounts used of components A.1) to A.6) are so dimensioned that per val hydroxyl groups 0.45 to 0.95, preferably 0.55 to 0.90, particularly preferably 0.65 to 0.85 Val isocyanate groups come.
Bevorzugt erfolgt die Herstellung der ionisch modifizierte, hydroxylgruppenhaltige Polyurethane und/oder Polyurethanharnstoffe (II) ohne Zusatz von organischen Lösemitteln.Preferably, the preparation of the ionically modified, hydroxyl-containing polyurethanes and / or polyurethane ureas (II) without addition of organic solvents.
Die im Prepolymer eingebauten Säuregruppen werden zumindest anteilig neutralisiert. Dies kann während oder auch nach der Prepolymerherstellung aber auch während oder nach der Dispergierung in Wasser durch Zugabe geeigneter Neutralisationsmittel (siehe auch bei PUR-Dispersion (I)) erfolgen. Beispiele für geeignete Neutralisationsmittel sind Triethylamin, Triethanolamin, Dimethylethanolamin, Ethyldiisopropylamin oder Diisopropylethylamin. Das Neutralisationsmittel wird zumeist im Molverhältnis zu den Säuregruppen des Prepolymers von 0,3:1 bis 1,3:1, bevorzugt von 0,6:1 bis 1,1:1 eingesetzt.The acid groups incorporated in the prepolymer are at least partially neutralized. This can be done during or after the prepolymer but also during or after the dispersion in water by adding suitable neutralizing agent (see also in PU dispersion (I)). Examples of suitable neutralizing agents are triethylamine, triethanolamine, dimethylethanolamine, ethyldiisopropylamine or diisopropylethylamine. The neutralizing agent is usually used in molar ratio to the acid groups of the prepolymer of 0.3: 1 to 1.3: 1, preferably from 0.6: 1 to 1.1: 1.
Anschließend wird das hydroxylgruppenfunktionelle Polyurethan durch Zugabe von Wasser oder durch Eintragen in Wasser in eine wässrige Dispersion überführt.Subsequently, the hydroxyl-functional polyurethane is converted by the addition of water or by adding in water in an aqueous dispersion.
Die Harze der nach dem vorhergehend beschriebenen Vorgehensweise erhältlichen PUR-Polymere (II) besitzen ein zahlenmittleres Molekulargewicht Mn von 1 000 bis 30 000 Da, bevorzugt von 1 500 bis 10 000 Da, eine Säurezahl von 10 bis 80, bevorzugt von 15 bis 40 mg KOH/g und einen Hydroxylgruppengehalt von 0,5 bis 6 Gew.-%, bevorzugt von 1,0 bis 4 Gew.-%.The resins of the polyurethane polymers (II) obtainable by the procedure described above have a number-average molecular weight M n of from 1,000 to 30,000 Da, preferably from 1,500 to 10,000 Da, an acid number of from 10 to 80, preferably from 15 to 40 mg KOH / g and a hydroxyl group content of 0.5 to 6 wt .-%, preferably from 1.0 to 4 wt .-%.
Die PUR-Dispersionen (I) und (II) können darüber hinaus alle für PUR-Dispersionen bekannten Additive wie beispielsweise Antioxidantien, Lichtschutzmittel und/oder andere Hilfs- und Zusatzmittel sowie Füllstoffe enthalten.The PU dispersions (I) and (II) may additionally contain all additives known for PU dispersions, such as, for example, antioxidants, light stabilizers and / or other auxiliaries and additives as well as fillers.
In den erfindungsgemäßen Beschichtungsmitteln sind auch Vernetzer (III) enthalten. Je nach Wahl des Vernetzer können sowohl Einkomponentenlacke als auch Zweikomponentenlacke hergestellt werden. Unter Einkomponentenlacken im Sinne der vorliegenden Erfindung sind dabei Überzugsmittel zu verstehen, bei denen Bindemittelkomponente und Vernetzerkomponente zusammen gelagert werden können, ohne dass eine Vernetzungsreaktion in merklichen bzw. für die spätere Applikation schädlichen Ausmaß stattfindet. Unter Zweikomponentenlacken im Sinne der vorliegenden Erfindung versteht man Überzugsmittel, bei denen Bindemittelkomponente und Vernetzerkomponente aufgrund ihrer hohen Reaktivität in getrennten Gefäßen gelagert werden müssen. Die beiden Komponenten werden erst kurz vor Applikation gemischt und reagieren dann im Allgemeinen ohne zusätzliche Aktivierung. Geeignete Vernetzer III) sind beispielsweise blockierte oder unblockierte Polyisocyanat-Vernetzer, Amid- und Amin-Formaldehydharze, Phenolharze, Aldehyd- und Ketonharze, wie z.B. Phenol-Formaldehydharze, Resole, Furanharze, Harnstoffharze, Carbamidsäureesterharze, Triazinharze, Melaminharze, Benzoguanaminharze, Cyanamidharze oder Anilinharze. Bevorzugt sind Polyisocyanate.Crosslinkers (III) are also present in the coating compositions according to the invention. Depending on the choice of crosslinker, both one-component and two-component coatings can be prepared. In the context of the present invention, one-component paints are to be understood as coating agents in which binder component and crosslinker component can be stored together, without a crosslinking reaction taking place in appreciable or detrimental extent for the subsequent application. Two-component coatings in the context of the present invention are understood to mean coating compositions in which binder component and crosslinker component must be stored in separate vessels because of their high reactivity. The two components are mixed just before application and then generally react without additional activation. Suitable crosslinkers III) include, for example, blocked or unblocked polyisocyanate crosslinkers, amide and amine-formaldehyde resins, phenolic resins, aldehyde and ketone resins, e.g. Phenol-formaldehyde resins, resoles, furan resins, urea resins, carbamic acid ester resins, triazine resins, melamine resins, benzoguanamine resins, cyanamide resins or aniline resins. Preference is given to polyisocyanates.
Besonders bevorzugt werden als Vernetzer-Komponente (III) Polyisocyanate mit freien IsocyanatGruppen eingesetzt, da die erhaltenen wässrigen Polyurethanlacke ein besonders hohes lacktechnische Niveau zeigen. Geeignete Vernetzer (III) sind beispielsweise Lackpolyisocyanate wie Uretdion-, Biuret-, Isocyanurat- oder Iminooxadiazindiongruppen aufweisenden Polyisocyanaten von Hexamethylendiisocyanat, 1-Isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexan oder Bis-(4-isocyanatocyclohexan)-methan.Polyisocyanates with free isocyanate groups are particularly preferably used as crosslinker component (III), since the resulting aqueous polyurethane coatings show a particularly high paint-technical level. Suitable crosslinkers (III) are, for example, paint polyisocyanates such as uretdione, biuret, isocyanurate or iminooxadiazinedione polyisocyanates of hexamethylene diisocyanate, 1-isocyanato-3,3,5-trimethyl-5-isocyanatomethylcyclohexane or bis (4-isocyanatocyclohexane) methane.
Ebenfalls Gegenstand der vorliegenden Erfindung ist ein Zweikomponenten-Lack, enthaltend die erfindungsgemäßen Beschichtungsmittel.Likewise provided by the present invention is a two-component coating comprising the coating compositions according to the invention.
Die hier beschriebenen PUR-Polymere (I) und (II) sind im Allgemeinen ausreichend hydrophil, so dass die Dispergierbarkeit auch hydrophober Vernetzer aus Komponente (III) gewährleistet ist. Falls gewünscht können aber auch zusätzliche externe Emulgatoren wie sie dem Fachmann bekannt sind zugesetzt werden.The PUR polymers (I) and (II) described here are generally sufficiently hydrophilic so that the dispersibility of hydrophobic crosslinkers of component (III) is ensured. If desired, however, it is also possible to add additional external emulsifiers as are known to the person skilled in the art.
Es können aber auch wasserlösliche bzw. dispergierbare Polyisocyanate wie sie z.B. durch Modifikation mit Carboxylat-, Sulfonat- und/oder Polyethylenoxidgruppen und/oder Polyethylenoxid/Polypropylenoxidgruppen erhältlich sind in Komponente (III) eingesetzt werden.However, it is also possible to use water-soluble or dispersible polyisocyanates, as described, for example, in US Pat. obtainable by modification with carboxylate, sulfonate and / or polyethylene oxide groups and / or polyethylene oxide / polypropylene oxide groups are used in component (III).
Prinzipiell möglich ist natürlich auch der Einsatz von Mischungen verschiedener Vernetzerharze der vorstehend genannten Art in der Komponente (III).In principle, of course, it is also possible to use mixtures of different crosslinker resins of the abovementioned type in component (III).
Ebenfalls Gegenstand der vorliegenden Erfindung ist ein Verfahren zur Herstellung der erfindungsgemäßen wässrigen Beschichtungsmitteln, dadurch gekennzeichnet, dass die PUR-Polymere (I) sowie die PUR-Polymere (II) in Wasser dispergiert und mit dem Vernetzer (III) vermischt werden.Likewise provided by the present invention is a process for preparing the aqueous coating compositions according to the invention, characterized in that the PU polymers (I) and the PU polymers (II) are dispersed in water and mixed with the crosslinker (III).
Das Verhältnis des Vernetzers (III) zu den mit ihm reaktiven Verbindungen der Komponenten (II) ist so zu wählen, dass ein Verhältnis von gegenüber dem Vernetzer reaktiven Gruppen aus (II) (z.B. OH-Gruppen) zu den reaktiven Gruppen des Vernetzers (bei Isocyanaten NCO-Gruppen) von 0,5 : 1,0 bis 3,5 : 1,0, bevorzugt 1,0 : 1,0 bis 3,0 : 1,0 und besonders bevorzugt von 1,0 : 1,0 bis 2,5 : 1,0 resultiert.The ratio of the crosslinker (III) to the compounds of the components (II) which are reactive with it should be selected such that a ratio of crosslinker-reactive groups from (II) (eg OH groups) to the reactive groups of the crosslinker (at Isocyanate NCO groups) of 0.5: 1.0 to 3.5: 1.0, preferably 1.0: 1.0 to 3.0: 1.0, and more preferably 1.0: 1.0 to 2.5: 1.0 results.
Die Mischung der Komponenten (I) und (II) enthält bevorzugt 5 bis 95 Gew.-% (bzgl. Festharz), besonders bevorzugt 25 bis 75 Gew.-% (bzgl. Festharz) der Komponente (II), wobei die Menge von (I) so zu wählen ist, dass die Gesamtmengen von (I) und (II) sich zu 100 Gew.-% (bzgl. Festharz) aufaddieren.The mixture of components (I) and (II) contains preferably from 5 to 95% by weight (with respect to solid resin), more preferably from 25 to 75% by weight (with respect to solid resin) of component (II), the amount of (I) is to be chosen so that the total amounts of (I) and (II) add up to 100 wt .-% (in terms of solid resin).
Als lackübliche Hilfs- und Zusatzmittel können in den erfindungsgemäßen Beschichtungsmitteln die dem Fachmann bekannten Stoffe wie Entschäumungsmittel, Verdickungsmittel, Pigmente, Dispergierhilfsmittel, Mattierungsmittel, Katalysatoren, Hautverhinderungsmittel, Antiabsetzmittel und/oder Emulgatoren, sowie Additive, die den gewünschten Softfeel-Effekt verstärken, enthalten sein. Dabei ist es unerheblich zu welchem Zeitpunkt der Herstellung diese den erfindungsgemäßen Beschichtungsmitteln zugesetzt oder in diese eingearbeitet werden.As customary auxiliaries and additives, the substances known to the person skilled in the art, such as defoaming agents, thickeners, pigments, dispersants, matting agents, catalysts, anti-skinning agents, anti-settling agents and / or emulsifiers, as well as additives which enhance the desired soft-feel effect, may be present in the coating compositions of the invention be. It is irrelevant at what point in the production of these added to the coating compositions of the invention or incorporated into this.
Die erfindungsgemäßen, wässrigen Beschichtungsmittel eignen sich für alle Einsatzgebiete, in denen wässrige Anstrich- und Beschichtungssysteme mit hohen Anforderungen an die Oberflächengüte Beständigkeit der Filme Verwendung finden, z.B. Beschichtung mineralischer Baustoff-Oberflächen, Lackierung und Versiegelung von Holz und Holzwerkstoffen, Beschichtung metallischer Oberflächen (Metallbeschichtung), Beschichtung und Lackierung asphalt- oder bitumenhaltiger Beläge, Lackierung und Versiegelung diverser Kunststoffoberflächen (Kunststoffbeschichtung) sowie als Hochglanzlacke.The aqueous coating compositions according to the invention are suitable for all fields of use in which aqueous coating and coating systems with high surface finish requirements of the films are used, e.g. Coating of mineral building material surfaces, painting and sealing of wood and wood-based materials, coating of metallic surfaces (metal coating), coating and coating of asphalt or bitumen-containing coatings, varnishing and sealing of various plastic surfaces (plastic coating) as well as high-gloss coatings.
Eine bevorzugte Verwendung der erfindungsgemäßen Beschichtungsmittel ist aber die Herstellung von Softfeel-Effektlacken, die gute Hydrolysebeständigkeiten bei sehr guten haptischen Eigenschaften gewährleisten. Bevorzugt werden solche Beschichtungsmittel in der Kunststofflackierung oder der Holzlackierung eingesetzt, wobei die Aushärtung üblicherweise bei Temperaturen zwischen Raumtemperatur und 130°C erfolgt. Die Zweikomponenten-Technologie mit nicht-blockierten Polyisocyanaten als Vernetzer erlaubt dabei die Verwendung vergleichsweise niedriger Aushärtetemperaturen in o.g. Intervall.However, a preferred use of the coating compositions according to the invention is the production of soft feel effect paints, which ensure good hydrolysis resistances with very good haptic properties. Such coating compositions are preferably used in the plastic coating or in the wood finish, wherein the curing usually takes place at temperatures between room temperature and 130 ° C. The two-component technology with non-blocked polyisocyanates as crosslinker allows the use of comparatively low curing temperatures in o.g. Interval.
Somit sind Softfeel-Lacke, enthaltend die erfindungsgemäßen Beschichtungsmittel ebenfalls Gegenstand der vorliegenden Erfindung.Thus softfeel paints containing the coating compositions according to the invention are likewise provided by the present invention.
Die erfindungsgemäßen, wässrigen Beschichtungsmittel werden üblicherweise in Einschichtlacken oder in der Klar- oder Decklackschicht (oberste Schicht) von Mehrschichtaufbauten eingesetzt.The aqueous coating compositions of the invention are usually used in single-coat paints or in the clearcoat or topcoat (top coat) of multi-layered structures.
Die Herstellung der Beschichtung kann nach den unterschiedlichen Spritzverfahren wie beispielsweise Luftdruck-, Airless- oder Elektrostatik-Spritzverfahren unter Verwendung von Ein-oder gegebenenfalls Zweikomponenten-Spritzanlagen erfolgen. Die Lacke und Beschichtungsmittel, enthaltend die erfindungsgemäßen Bindemitteldispersionen, können jedoch auch nach anderen Methoden, beispielsweise durch Streichen, Rollen oder Rakeln appliziert werden.The preparation of the coating can be carried out by the different injection methods such as air pressure, airless or electrostatic spray method using single or optionally two-component spray systems. However, the lacquers and coating compositions containing the binder dispersions according to the invention can also be applied by other methods, for example by brushing, rolling or knife coating.
Gegenstand der vorliegenden Erfindung ist ebenfalls ein Mehrschichtenaufbau, dadurch gekennzeichnet, dass die oberste Schicht, die eine Klar- oder Decklackschicht ist, einen Softfeel-Lack, enthaltend die erfindungsgemäßen Beschichtungsmittel, enthält.The present invention likewise relates to a multilayer structure, characterized in that the topmost layer, which is a clear or topcoat layer, contains a softfeel lacquer containing the coating compositions according to the invention.
Soweit nicht abweichend angegeben sind alle Prozentangaben als Gewichtsprozent zu verstehen.Unless otherwise indicated, all percentages are by weight.
- Diaminosulfonat:diaminosulphonate:
- NH2-CH2CH2-NH-CH2CH2-SO3Na (45 %ig in Wasser)NH 2 -CH 2 CH 2 -NH-CH 2 CH 2 -SO 3 Na (45% in water)
- Desmophen® 3600:Desmophen ® 3600:
- difunktioneller Polyether auf Propylenoxidbasis, zahlenmittleres Molekulargewicht 2000 g/mol, OH-Zahl 56 mg KOH/g (Bayer AG, Leverkusen, DE)Difunctional polyether based on propylene oxide, number average molecular weight 2000 g / mol, OH number 56 mg KOH / g (Bayer AG, Leverkusen, DE)
- Polyether LB 25:Polyether LB 25:
- (monofunktioneller Polyether auf Ethylenoxid-/Propylenoxidbasis zahlenmittleres Molekulargewicht 2250 g/mol, OH-Zahl 25 mg KOH/g (Bayer AG, Leverkusen, DE)(monofunctional polyether based on ethylene oxide / propylene oxide number average molecular weight 2250 g / mol, OH number 25 mg KOH / g (Bayer AG, Leverkusen, DE)
- BYK® 348:BYK ® 348:
- Benetzungsmittel (BYK-Chemie, Wesel, DE)Wetting agent (BYK-Chemie, Wesel, DE)
- Tego-Wet® KL 245:Tego- Wet® KL 245:
- Verlaufsadditiv, 50 %ig in Wasser (Tegochemie, Essen, DE)Leveling additive, 50% in water (Tegochemie, Essen, DE)
- Aquacer® 535:Aquacer ® 535:
- Wachsemulsion (BYK-Chemie, Wesel, DE)Wax emulsion (BYK-Chemie, Wesel, DE)
- Entschäumer DNE:Defoamer DNE:
- Entschäumer (K. Obermayer, Bad Berleburg, DE)Defoamer (K. Obermayer, Bad Berleburg, DE)
- Sillitin® Z 86:Sillitin ® Z 86:
- Füllstoff (Hoffmann & Söhne, Neuburg, DE)Filler (Hoffmann & Söhne, Neuburg, DE)
- Talkum® IT extra:Talc ® IT extra:
- Mattierungsmittel (Norwegian Talc, Frankfurt, DE)Matting agent (Norwegian Talc, Frankfurt, DE)
- Bayferrox® 318 M:Bayferrox ® 318 M:
- Farbpigment (schwarz) (Bayer AG, Leverkusen, DE)Color pigment (black) (Bayer AG, Leverkusen, DE)
- OK 412:OK 412:
- Mattierungsmittel (Degussa, Frankfurt, DE)Matting agents (Degussa, Frankfurt, DE)
- Bayhydur®3100:Bayhydur® ® 3100:
- Hydrophiles, aliphatisches Polyisocyanat auf Basis Hexamethylendiisocyanat (HDI) mit einem Isocyanatgehalt von 17,4 % (Bayer AG, Leverkusen, DE)Hydrophilic, aliphatic polyisocyanate based on hexamethylene diisocyanate (HDI) with an isocyanate content of 17.4% (Bayer AG, Leverkusen, DE)
- MPA:MPA:
- 1-Methoxy-2-propylacetat1-methoxy-2-propyl
Die Bestimmung der Festkörpergehalte erfolgte nach DIN-EN ISO 3251.The solids contents were determined according to DIN-EN ISO 3251.
NCO-Gehalte wurden, wenn nicht ausdrücklich anders erwähnt, volumetrisch gemäß DIN-EN ISO 11909 bestimmt.NCO contents were determined volumetrically in accordance with DIN-EN ISO 11909, unless expressly stated otherwise.
In ein 151-Reaktionsgefäß mit Rührer, Heizvorrichtung und Wasserabscheider mit Kühlvorrichtung wurden 1281 g Phthalsäureanhydrid, 5058 g Adipinsäure, 6387 g Hexandiol-1,6 und 675 g Neopentylglykol eingewogen und unter Stickstoff in einer Stunde auf 140°C aufgeheizt. In weiteren 9 Stunden wurde auf 220°C aufgeheizt und so lange bei dieser Temperatur kondensiert, bis eine Säurezahl kleiner 3 erreicht war. Das so erhaltene Polyesterpolyol hatte eine Viskosität (bestimmt als Auslaufzeit einer 80 %igen Lösung des Polyesters in Methoxypropylacetat im DIN 4-Becher bei 23°C) von 54 Sekunden und eine OH-Zahl von 160 mg KOH/g.In a 151-reaction vessel with stirrer, heater and water with a condenser, 1281 g of phthalic anhydride, 5058 g of adipic acid, 6387 g of 1,6-hexanediol and 675 g of neopentyl glycol were weighed and heated to 140 ° C under nitrogen in one hour. In a further 9 hours was heated to 220 ° C and condensed at this temperature until an acid number less than 3 was reached. The polyesterpolyol thus obtained had a viscosity (determined as the flow time of an 80% strength solution of the polyester in methoxypropyl acetate in the DIN 4 cup at 23 ° C.) of 54 seconds and an OH number of 160 mg KOH / g.
1223 g 1,4-Butandiol und 535 g 1,6 Hexandiol wurden in einem Kolben vorgelegt und auf 100°C aufgeheizt. Schließlich wurden ca. 2 1/h Stickstoff in das Diolgemisch eingeleitet und 20 mbar Vakuum angelegt und das Gemisch solange entwässert (ca. 2 Stunden), bis der Wassergehalt ≤ 0,1 % betrug.1,223 g of 1,4-butanediol and 535 g of 1,6-hexanediol were placed in a flask and heated to 100 ° C. Finally, about 2 1 / h nitrogen were introduced into the diol and 20 mbar vacuum applied and the mixture as long dehydrated (about 2 hours) until the water content was ≤ 0.1%.
Danach wurden 0,44 g Ytterbium(III)acetylacetonat zugegeben, das Diolgemisch auf 110°C aufgeheizt. Anschließend wurden in ca. 20 Minuten 2297 g Dimethylcarbonat zulaufen lassen und das Reaktionsgemisch 24 h unter Rückfluß gehalten. Schließlich wurde die Temperatur auf 150°C erhöht und anfallendes Destillat entfernt. Danach erfolgte eine weitere Erhöhung auf 180°C gefolgt von einer weiteren Destillationsphase.Thereafter, 0.44 g of ytterbium (III) acetylacetonate were added, the diol mixture was heated to 110 ° C. Then 2297 g of dimethyl carbonate were run in about 20 minutes and kept the reaction mixture under reflux for 24 h. Finally, the temperature was raised to 150 ° C and any distillate was removed. This was followed by a further increase to 180 ° C followed by another distillation phase.
Das Reaktionsgemisch wurde auf 130°C abgekühlt und der Druck auf 10 mbar gesenkt. Anschließend erfolgte eine Anhebung der Ölbadtemperatur von 130°C auf 180°C binnen 2 h, wobei die Destillationskopftemperatur 60°C nicht überstieg. Nach Erreichen von 180°C wurde diese Temperatur 6 h gehalten.The reaction mixture was cooled to 130 ° C and the pressure was lowered to 10 mbar. This was followed by an increase in the oil bath temperature from 130 ° C to 180 ° C within 2 h, the distillation head temperature did not exceed 60 ° C. After reaching 180 ° C, this temperature was maintained for 6 h.
Anschließend wurde das Reaktionsgemisch auf 130°C abgekühlt und der Druck auf 10 mbar gesenkt. Danach erfolgte eine Anhebung der Ölbadtemperatur von 130°C auf 180°C binnen 2 h, wobei die Destillationskopftemperatur 60°C nicht überstieg. Nach Erreichen von 180°C wurde diese Temperatur 6 h gehalten. Das Reaktionsgemisch wurde auf Raumtemperatur abgekühlt und die Kenndaten des Produktes bestimmt.Subsequently, the reaction mixture was cooled to 130 ° C and the pressure was lowered to 10 mbar. This was followed by an increase in the oil bath temperature from 130 ° C to 180 ° C within 2 h, the distillation head temperature did not exceed 60 ° C. After reaching 180 ° C, this temperature was maintained for 6 h. The reaction mixture was cooled to room temperature and the characteristics of the product determined.
Es wird ein Polycarbonatdiol mit einer Hydroxylzahl von 57,3 mg KOH/g sowie einer Viskosität von 115 Pas bei 23°C erhalten.A polycarbonate diol having a hydroxyl number of 57.3 mg KOH / g and a viscosity of 115 Pas at 23 ° C. is obtained.
1239 g 1,4-Butandiol und 542 g 1,6 Hexandiol wurden in einem Kolben vorgelegt und auf 100°C im Ölbad aufgeheizt. Schließlich wurden ca. 2 l/h Stickstoff in das Diolgemisch eingeleitet und 20 mbar Vakkum angelegt und das Gemisch solange entwässert (ca. 2 Stunden) bis der Wassergehalt ≤ 0,1% betrug.1239 g of 1,4-butanediol and 542 g of 1,6-hexanediol were placed in a flask and heated to 100 ° C in an oil bath. Finally, about 2 l / h of nitrogen were introduced into the diol mixture and 20 mbar Vakkum applied and the mixture as long dehydrated (about 2 hours) until the water content was ≤ 0.1%.
Danach wurden 0,44 g Ytterbium(III)acetylacetonat zugegeben das Diolgemisch auf 110°C aufgeheizt. Anschließend wurden in ca. 20 Minuten 2180 g Dimethylcarbonat zulaufen lassen und das Reaktionsgemisch 24 h unter Rückfluß gehalten. Schließlich wurde die Temperatur auf 150°C erhöht und anfallendes Destillat entfernt. Danach erfolgte eine weitere Erhöhung auf 180°C gefolgt von einer weiteren Destillationsphase.Thereafter, 0.44 g of ytterbium (III) acetylacetonate added, the diol mixture was heated to 110 ° C. Then 2180 g of dimethyl carbonate were allowed to run in about 20 minutes and the reaction mixture was refluxed for 24 h. Finally, the temperature was raised to 150 ° C and any distillate was removed. This was followed by a further increase to 180 ° C followed by another distillation phase.
Das Reaktionsgemisch wurde auf 130°C abgekühlt und der Druck auf 10 mbar gesenkt. Anschließend erfolgte eine Anhebung der Ölbadtemperatur von 130°C auf 180°C binnen 2 h, wobei die Destillationskopftemperatur 60°C nicht überstieg. Nach Erreichen von 180°C wurde diese Temperatur 6 h gehalten.The reaction mixture was cooled to 130 ° C and the pressure was lowered to 10 mbar. This was followed by an increase in the oil bath temperature from 130 ° C to 180 ° C within 2 h, the distillation head temperature did not exceed 60 ° C. After reaching 180 ° C, this temperature was maintained for 6 h.
Anschließend wurde das Reaktionsgemisch auf 130°C abgekühlt und der Druck auf 10 mbar gesenkt. Danach erfolgte eine Anhebung der Ölbadtemperatur von 130°C auf 180°C binnen 2 h, wobei die Destillationskopftemperatur 60°C nicht überstieg. Nach Erreichen von 180°C wurde diese Temperatur 6 h gehalten. Danach wurde das Reaktionsgemisch auf Raumtemperatur abgekühlt und die Kenndaten des Produktes bestimmt.Subsequently, the reaction mixture was cooled to 130 ° C and the pressure was lowered to 10 mbar. This was followed by an increase in the oil bath temperature from 130 ° C to 180 ° C within 2 h, the distillation head temperature did not exceed 60 ° C. After reaching 180 ° C, this temperature was maintained for 6 h. Thereafter, the reaction mixture was cooled to room temperature and the characteristics of the product determined.
Es wird ein Polycarbonatdiol mit einer Hydroxylzahl von 113,4 mg KOH/g sowie einer Viskosität von 13600 mPas bei 23°C erhalten.There is obtained a polycarbonate diol having a hydroxyl number of 113.4 mg KOH / g and a viscosity of 13600 mPas at 23 ° C.
- Bayhydrol® PR 240:Bayhydrol ® PR 240:
- anionisch hydrophilierte PUR-Dispersion auf Polyesterbasis mit einem Festkörpergehalt von 40 % und einer mittleren Teilchengröße von 100-300 nm (Bayer AG, Leverkusen, DE)anionically hydrophilicized PUR dispersion based on polyester with a solids content of 40% and an average particle size of 100-300 nm (Bayer AG, Leverkusen, DE)
- Bayhydrol® PR 340:Bayhydrol ® PR 340:
- anionisch hydrophilierte PUR-Dispersion auf Basis eines Polycarbonatdiols, welches ausschließlich 1,6-Hexandiol als Diol-Aufbaukomponente erhält, mit einem Festkörpergehalt von 50 % und einer mittleren Teilchengröße von 100-300 nm (Bayer AG, Leverkusen, DE)anionically hydrophilic PUR dispersion based on a polycarbonate diol which only 1,6-hexanediol as a diol-building component, with a solids content of 50% and an average particle size of 100-300 nm (Bayer AG, Leverkusen, DE)
64,0 g Desmophen® 3600, 196,8 g Beispiel 2, und 10,9 g Polyether LB 25 wurden auf 75°C aufgeheizt. Anschließend wurde bei 75°C innerhalb von 5 min 48,7 g Hexamethylendiisocanat zugegeben, auf 100°C aufgeheizt und solange bei 100°C gerührt, bis der theoretische NCO-Wert erreicht wurde. Das fertige Prepolymer wurde mit 568,1 g Aceton bei 50°C gelöst und anschließend eine Lösung aus 1,2 g Hydrazinhydrat, 7,70 g Diaminosulfonat, 2,20 g 1,2-Diaminoethan und 82,3 g Wasser innerhalb von 5 min zudosiert. Die Nachrührzeit betrug 30 min. Die Dispergierung erfolgte durch Zugabe von 408,4g Wasser. Nach Entfernung des Lösemittels durch Destillation im Vakuum wurde keine lagerstabile Dispersion mit einem Festkörpergehalt von 40,0 % erhalten.64.0 g Desmophen ® 3600, 196.8 g of Example 2 and 10.9 g of polyether LB 25 were heated to 75 ° C. Subsequently, 48.7 g of hexamethylene diisocyanate was added at 75 ° C within 5 min, heated to 100 ° C and stirred at 100 ° C until the theoretical NCO value was reached. The finished prepolymer was dissolved with 568.1 g of acetone at 50 ° C and then a solution of 1.2 g of hydrazine hydrate, 7.70 g of diaminosulfonate, 2.20 g of 1,2-diaminoethane and 82.3 g of water within 5 min. The stirring time was 30 min. The dispersion was carried out by adding 408.4 g of water. After removal of the solvent by distillation in vacuo, no storage-stable dispersion having a solids content of 40.0% was obtained.
Bayhydrol® XP 2429: Aliphatische hydroxyfunktionelle Polyesterpolyurethan-Dispersion des Stands der Technik, hergestellt unter Verwendung eines Polycarbonatdiols, welches ausschließlich auf 1,6-Hexandiol als Diolkomponente basiert, mit einem Festkörpergehalt von 55 % (Bayer AG, Leverkusen, DE)Bayhydrol ® XP 2429: aliphatic hydroxy-functional polyester-polyurethane dispersion of the prior art produced by using a polycarbonate diol, which is based solely on 1,6-hexanediol as the diol component, having a solids content of 55% (Bayer AG, Leverkusen, DE)
In einem 61-Reaktionsgefäß mit Kühl-, Heiz- und Rührvorrichtung wurden in einer Stickstoffatmosphäre 1170 g des Polyesterpolyols aus Beispiel 1 vorgelegt und zusammen mit 1140 g Polycarbonatdiol aus Beispiel 2, 90 g Trimethylolpropan, 120 g Dimethylolpropionsäure und 3,8 g Zinn-(II)-octoat auf 130°C aufgeheizt und 30 min homogenisiert. Anschließend wurde auf 80°C abgekühlt, 480 g Hexamethylendiisocyanat unter kräftigen Rühren zugegeben, unter Ausnutzung der Exothermie auf 140°C aufgeheizt und das Gemisch solange bei dieser Temperatur gehalten, bis sich keine NCO-Gruppen mehr feststellen ließen.In a 61 reaction vessel with cooling, heating and stirring device 1170 g of the polyester polyol from Example 1 were initially charged in a nitrogen atmosphere and together with 1140 g of polycarbonate diol from Example 2, 90 g of trimethylolpropane, 120 g of dimethylolpropionic acid and 3.8 g of tin ( II) -octoate heated to 130 ° C and homogenized for 30 min. The mixture was then cooled to 80 ° C, 480 g of hexamethylene diisocyanate added with vigorous stirring, heated to 140 ° C using the exotherm and the mixture kept at this temperature until no more NCO groups could be determined.
Anschließend wurde das so erhaltene Polyurethan auf 90°-100°C abgekühlt, 47 g Dimethylethanolamin (Neutralisationsgrad 60 %) zugesetzt, 15 Minuten homogenisiert und mit 2270 g demineralisiertem Wasser dispergiert. Die so erhaltene wässrige Polyurethanharz-Dispersion hatte einen OH-Gehalt (100 %ig) von 1,4 %, eine Säurezahl (100 %ig) von 16,8, eine mittlere Teilchengröße von 110 nm und eine Viskosität von ca. 2020 mPas (23°C; D = 40 s-1) bei einem Festkörpergehalt von 51,2 Gew.-%.Subsequently, the polyurethane thus obtained was cooled to 90 ° -100 ° C, 47 g of dimethylethanolamine (degree of neutralization 60%) was added, homogenized for 15 minutes and dispersed with 2270 g of demineralized water. The resulting aqueous polyurethane resin dispersion had an OH content (100%) of 1.4%, an acid number (100%) of 16.8, an average particle size of 110 nm and a viscosity of about 2020 mPas ( 23 ° C, D = 40 s -1 ) at a solids content of 51.2 wt .-%.
In einem 61-Reaktionsgefäß mit Kühl-, Heiz- und Rührvorrichtung wurden in einer Stickstoffatmosphäre 1170 g des Polyesterpolyols aus Beispiel 1 vorgelegt und zusammen mit 1140 g Polycarbonatdiol aus Beispiel 3, 90 g Trimethylolpropan, 120 g Dimethylolpropionsäure, 125 g N-Methylpyrrolidon und 3,8 g Zinn-(II)-octoat auf 130°C aufgeheizt und 30 min homogenisiert. Anschließend wurde auf 80°C abgekühlt, 480 g Hexamethylendiisocyanat unter kräftigen Rühren zugegeben, unter Ausnutzung der Exothermie auf 140°C aufgeheizt und das Gemisch solange bei dieser Temperatur gehalten, bis sich keine NCO-Gruppen mehr feststellen ließen.In a 61-reaction vessel with cooling, heating and stirring 1170 g of the polyester polyol from Example 1 were initially charged and together with 1140 g of polycarbonate diol from Example 3, 90 g of trimethylolpropane, 120 g of dimethylolpropionic acid, 125 g of N-methylpyrrolidone and 3 , 8 g of tin (II) octoate heated to 130 ° C and homogenized for 30 min. The mixture was then cooled to 80 ° C, 480 g of hexamethylene diisocyanate added with vigorous stirring, heated to 140 ° C using the exotherm and the mixture kept at this temperature until no more NCO groups could be determined.
Anschließend wurde das so erhaltene Polyurethan auf 90°-100°C abgekühlt, 39 g Dimethylethanolamin (Neutralisationsgrad 50 %) zugesetzt, 15 Minuten homogenisiert mit 2270 g demineralisiertem Wasser dispergiert. Die so erhaltene wässrige Polyurethanharz-Dispersion hatte einen OH-Gehalt (100 %ig) von 1,4 %, eine Säurezahl (100 %ig) von 16,3, eine mittlere Teilchengröße von 150 nm und eine Viskosität von ca. 1680 mPas (23°C; D = 40 s-1) bei einem Festkörpergehalt von 55,9 Gew.-%.Subsequently, the polyurethane thus obtained was cooled to 90 ° -100 ° C, 39 g dimethylethanolamine (degree of neutralization 50%) was added, homogenized for 15 minutes with 2270 g of demineralized water. The aqueous polyurethane resin dispersion thus obtained had an OH content (100%) of 1.4%, an acid number (100%) of 16.3, an average particle size of 150 nm and a viscosity of about 1680 mPas ( 23 ° C, D = 40 s -1 ) at a solids content of 55.9 wt .-%.
Mit den Beispielen 1-9 werden folgende anwendungstechnische Versuche zur Herstellung von Softfeel Beschichtungen durchgeführt:Examples 1-9 are used for the following performance tests for the production of softfeel coatings:
Die Herstellung des Stammlackes erfolgt nach Vordispergierung durch Anreibung über einen Laborschüttler. Die Temperatur des Mahlgutes sollte 40°C nicht überschreiten. Anschließend OK 412 ca. 10 min. einrühren. Nach Vernetzung wird das Lacksystem auf ca. 30 s Auslaufzeit (DIN ISO 2431, 5mm Düse) eingestellt und konventionell auf Bayblend® T 65 verspritzt. Die Trockenfilmschichtdicke beträgt zwischen 30 und 40 µm.
Trocknungsbedingung: 10 min / RT, 30 min / 80°C und ca. 16h / 60°C Alterung
Trocknungsbedingung: 10 min / RT, 30 min / 80°C und ca. 16h / 60°C Alterung
Die Bleistifthärtemethode ist eine Prüfung zur Ermittlung der Lackfilmhärte. Es werden Bleistifte unterschiedlichen Härte (6B bis 7H) an lackierten Prüfkörpern wie folgt bei Raumtemperatur getestet: Die Bleistiftspitze wird horizontal geschliffen, so dass sich eine plane, runde Fläche ergibt. In einem Winkel von 45 ° wird der Bleistift anschließend über den zu prüfenden Lackfilm geschoben, wobei eine möglichst gleichbleibende Kraft aufgebracht werden sollte. Der Wert der Bleistifthärte ist ermittelt, wenn die Lackoberfläche zum ersten Mal eine Schädigung aufweist.
2 bestimmt nach DIN EN ISO 2409 (O = bester Wert, 5 = schlechtester Wert)
3 Prüfung der Filmerweichung (Fingemagelprobe):
Die Filmerweichung wird mit Hilfe der Filmnagelprobe bestimmt. Die Beurteilung der Erweichung durch die Fingernagelprobe ist wie folgt:
nicht verkratzbar = 0 (bester Wert) bis auf den Untergrund durchkratzbar = 5 (schlechtester Wert)
Alle Beschichtungen gemäß der Beispiel 10-17 weisen eine vergleichbare Härte und exzellente Haptik auf. Die Ergebnisse aus Tabelle 3 belegen aber, dass im Gegensatz zu den erfindungsgemäßen Beschichtungen (Beispiel 16-17) nach 72 h unter Hydrolyse bei 90°C und 90 % relativer Luftfeuchte die Vergleichsbeispiele jedoch erhebliche Filmerweichungen (Abbau durch Hydrolyse (Vergleiche Tabelle 3 Spalte B-Härte /Erweichung)) aufweisen, wohingegen die Beschichtungen aus den erfindungsgemäßen Beispielen 16-17 keinerlei Erweichung zeigen, d.h signifikant hydrolysestabiler sind.
Drying condition: 10 min / RT, 30 min / 80 ° C and approx. 16h / 60 ° C aging
Drying condition: 10 min / RT, 30 min / 80 ° C and approx. 16h / 60 ° C aging
The pencil hardening method is a test for determining the paint film hardness. Pencils of different hardness (6B to 7H) on painted specimens are tested at room temperature as follows: The pencil tip is ground horizontally to give a flat, round surface. At an angle of 45 °, the pencil is then pushed over the paint film to be tested, whereby a force that is as constant as possible should be applied. The value of pencil hardness is determined when the paint surface is damaged for the first time.
2 determined according to DIN EN ISO 2409 (O = best value, 5 = worst value)
3 Film softening test (fingernail test):
The film softening is determined by means of the film nail sample. The evaluation of the softening by the fingernail sample is as follows:
not scratchable = 0 (best value) scratch-through to the substrate = 5 (worst value)
All coatings according to Example 10-17 have a comparable hardness and excellent feel. However, the results from Table 3 show that, in contrast to the coatings of the invention (Example 16-17) after 72 h with hydrolysis at 90 ° C and 90% relative humidity, the comparative examples, however, significant film deviations (degradation by hydrolysis (Comparative Table 3 column B Hardness / softening)), whereas the coatings of Examples 16-17 according to the invention show no softening, ie are significantly more stable to hydrolysis.
Claims (12)
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DE102005029626A DE102005029626A1 (en) | 2005-06-23 | 2005-06-23 | Polymer mixture based on polycarbonate polyols |
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EP (1) | EP1736490B1 (en) |
JP (1) | JP2007002248A (en) |
KR (1) | KR20060134854A (en) |
CN (1) | CN1884408A (en) |
AT (1) | ATE442393T1 (en) |
BR (1) | BRPI0602330A (en) |
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WO2011075718A1 (en) | 2009-12-18 | 2011-06-23 | E. I. Du Pont De Nemours And Company | Water-based coating compositions |
WO2014004598A2 (en) | 2012-06-26 | 2014-01-03 | U.S. Coatings Ip Co. Llc | Process for multi-layer coating |
US9273210B2 (en) | 2011-03-29 | 2016-03-01 | Covestro Deutschland Ag | Use of an aqueous preparation for the coating of wood surfaces to achieve a natural-touch effect |
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KR100828789B1 (en) * | 2006-07-05 | 2008-05-09 | 현대자동차주식회사 | Thinwall Waterborne Soft Feel Paint |
JP4407728B2 (en) * | 2007-08-07 | 2010-02-03 | Basfコーティングスジャパン株式会社 | Multi-layer coating formation method |
WO2009036151A2 (en) * | 2007-09-14 | 2009-03-19 | Lord Corporation | Clear functional coating for elastomers |
DE102007054002A1 (en) * | 2007-11-13 | 2009-05-14 | Bayer Materialscience Ag | Nonionic hydrophilicized binder dispersions |
KR101187118B1 (en) | 2007-11-16 | 2012-09-28 | 아사히 가세이 케미칼즈 가부시키가이샤 | Polycarbonate diol |
WO2010009993A1 (en) * | 2008-07-22 | 2010-01-28 | Basf Se | Polyurethane dispersion containing an alkanolamine |
JP5457039B2 (en) * | 2009-01-09 | 2014-04-02 | 旭化成ケミカルズ株式会社 | Curable composition for water-based soft-feel coatings with improved coating flexibility and resistance balance |
PT2488563E (en) * | 2009-10-15 | 2014-10-31 | Benecke Kaliko Ag | Use of nmp-free coatings for automotive interiors |
DE102009060552A1 (en) * | 2009-12-23 | 2011-06-30 | Bayer MaterialScience AG, 51373 | Polyurethane binder |
WO2012130764A1 (en) | 2011-03-29 | 2012-10-04 | Bayer Materialscience Ag | Use of an aqueous preparation for the coating of wood surfaces to achieve a natural-touch effect |
US8354151B1 (en) * | 2011-07-06 | 2013-01-15 | Bayer Materialscience Llc | Waterborne polyurethane coating compositions |
US20130011590A1 (en) * | 2011-07-06 | 2013-01-10 | Bayer Materialscience Ag | Waterborne polyurethane coating compositions |
WO2013034539A1 (en) * | 2011-09-07 | 2013-03-14 | Bayer Intellectual Property Gmbh | Polycarbonate polyols |
JP2014122323A (en) | 2012-10-31 | 2014-07-03 | Dow Global Technologies Llc | Polycarbonate coatings for metal packaging |
US9523021B2 (en) | 2014-04-25 | 2016-12-20 | Ppg Industries Ohio, Inc. | Waterborne coating compositions for soft touch coatings |
EP3100915B2 (en) | 2015-06-03 | 2022-09-28 | WEIDPLAS GmbH | Component |
JP2017165884A (en) * | 2016-03-17 | 2017-09-21 | 三洋化成工業株式会社 | Polyurethane resin water dispersion |
EP3235844A1 (en) * | 2016-04-20 | 2017-10-25 | ALLNEX AUSTRIA GmbH | Aqueous polyurethane dispersion |
WO2019093219A1 (en) * | 2017-11-07 | 2019-05-16 | Dic株式会社 | Heat-curable urethane resin composition, film, and article |
KR20200102985A (en) * | 2017-12-21 | 2020-09-01 | 코베스트로 도이칠란트 아게 | Adhesives based on specific polyurethaneurea with adjustable adhesive strength, preparation and use thereof |
US10689488B2 (en) * | 2018-01-02 | 2020-06-23 | Industrial Technology Research Institute | Method for preparing polycarbonate polyol and composition comprising the polycarbonate polyol |
CN111135120B (en) * | 2018-11-06 | 2021-04-20 | 万华化学集团股份有限公司 | Waterborne polyurethane functional surface film matrix and application thereof |
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- 2006-06-13 EP EP06012152A patent/EP1736490B1/en not_active Not-in-force
- 2006-06-20 CA CA002550470A patent/CA2550470A1/en not_active Abandoned
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- 2006-06-22 JP JP2006172389A patent/JP2007002248A/en not_active Withdrawn
- 2006-06-22 KR KR1020060056433A patent/KR20060134854A/en not_active Application Discontinuation
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Also Published As
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KR20060134854A (en) | 2006-12-28 |
DE102005029626A1 (en) | 2007-01-04 |
EP1736490A3 (en) | 2008-04-02 |
US20060293468A1 (en) | 2006-12-28 |
ES2330547T3 (en) | 2009-12-11 |
ATE442393T1 (en) | 2009-09-15 |
JP2007002248A (en) | 2007-01-11 |
CA2550470A1 (en) | 2006-12-23 |
DE502006004775D1 (en) | 2009-10-22 |
CN1884408A (en) | 2006-12-27 |
EP1736490B1 (en) | 2009-09-09 |
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EP2912079B1 (en) | Coating agent for coatings that can be matted |
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